PubMed Health⌕ Search

Biomedical subjects

B Witholt

Publications and source records attributed to B Witholt.

At least 37 records · Page 2Linked to original sources
PubMed2000

Development of an improved in vitro activity assay for medium chain length PHA polymerases based on CoenzymeA release measurements.

An improved activity assay for polyhydroxyalkanoate (PHA) polymerases from Pseudomonas oleovorans GPo1 was developed. The activity assay is based on the detection of released Coenzyme A (CoA) using 5,5'-dithiobis (2-nitrobenzoic acid) (DTNB), a compound which specifically reacts with thiol groups. The formed adduct was measured spectrophotometrically with high sensitivity and accuracy. The assay was used to study the effect of several additives on the activity of granule-associated PHA polymerase. Mild non-ionic detergents such as Tween-20, Triton X-100, CHAPS and Hecameg all appeared to be strongly inhibitory. In contrast, bovine serum albumin (BSA) had a strong stimulatory effect on the activity and stability of the PHA polymerases. Using optimized conditions, activities up to 5.8 U/mg granule-bound polymerase have been measured.

Acyltransferases↗
PubMed2000

Expression, stability and performance of the three-component alkane mono-oxygenase of Pseudomonas oleovorans in Escherichia coli.

We tested the synthesis and in vivo function of the inducible alkane hydroxylase of Pseudomonas oleovorans GPo1 in several Escherichia coli recombinants. The enzyme components (AlkB, AlkG and AlkT) were synthesized at various rates in different E. coli hosts, which after induction produced between twofold and tenfold more of the Alk components than did P. oleovorans. The enzyme components were less stable in recombinant E. coli hosts than in P. oleovorans. In addition, the specific activity of the alkane mono-oxygenase component AlkB was five or six times lower in E. coli than in P. oleovorans. Evidently, optimal functioning of the hydroxylase system requires factors or a molecular environment that are available in Pseudomonas but not in E. coli. These factors are likely to include correct interactions of AlkB with the membrane and incorporation of iron into the AlkG and AlkB apoproteins.

Cytochrome P-450 CYP4A↗
PubMed2000

Inactivation of isocitrate lyase leads to increased production of medium-chain-length poly(3-hydroxyalkanoates) in Pseudomonas putida.

Medium-chain-length (mcl) poly(3-hydroxyalkanoates) (PHAs) are storage polymers that are produced from various substrates and accumulate in Pseudomonas strains belonging to rRNA homology group I. In experiments aimed at increasing PHA production in Pseudomonas strains, we generated an mcl PHA-overproducing mutant of Pseudomonas putida KT2442 by transposon mutagenesis, in which the aceA gene was knocked out. This mutation inactivated the glyoxylate shunt and reduced the in vitro activity of isocitrate dehydrogenase, a rate-limiting enzyme of the citric acid cycle. The genotype of the mutant was confirmed by DNA sequencing, and the phenotype was confirmed by biochemical experiments. The aceA mutant was not able to grow on acetate as a sole carbon source due to disruption of the glyoxylate bypass and exhibited two- to fivefold lower isocitrate dehydrogenase activity than the wild type. During growth on gluconate, the difference between the mean PHA accumulation in the mutant and the mean PHA accumulation in the wild-type strain was 52%, which resulted in a significant increase in the amount of mcl PHA at the end of the exponential phase in the mutant P. putida KT217. On the basis of a stoichiometric flux analysis we predicted that knockout of the glyoxylate pathway in addition to reduced flux through isocitrate dehydrogenase should lead to increased flux into the fatty acid synthesis pathway. Therefore, enhanced carbon flow towards the fatty acid synthesis pathway increased the amount of mcl PHA that could be accumulated by the mutant.

Gluconates↗
PubMed2000

Properties of engineered poly-3-hydroxyalkanoates produced in recombinant Escherichia coli strains.

To prepare medium-chain-length poly-3-hydroxyalkanoates (PHAs) with altered physical properties, we generated recombinant Escherichia coli strains that synthesized PHAs with altered monomer compositions. Experiments with different substrates (fatty acids with different chain lengths) or different E. coli hosts failed to produce PHAs with altered physical properties. Therefore, we engineered a new potential PHA synthetic pathway, in which ketoacyl-coenzyme A (CoA) intermediates derived from the beta-oxidation cycle are accumulated and led to the PHA polymerase precursor R-3-hydroxyalkanoates in E. coli hosts. By introducing the poly-3-hydroxybutyrate acetoacetyl-CoA reductase (PhbB) from Ralstonia eutropha and blocking the ketoacyl-CoA degradation step of the beta-oxidation, the ketoacyl-CoA intermediate was accumulated and reduced to the PHA precursor. Introduction of the phbB gene not only caused significant changes in the monomer composition but also caused changes of the physical properties of the PHA, such as increase of polymer size and loss of the melting point. The present study demonstrates that pathway engineering can be a useful approach for producing PHAs with engineered physical properties.

3-Hydroxyacyl CoA Dehydrogenases↗
PubMed2000

Methods for intense aeration, growth, storage, and replication of bacterial strains in microtiter plates.

Miniaturized growth systems for heterogeneous culture collections are not only attractive in reducing demands for incubation space and medium but also in making the parallel handling of large numbers of strains more practicable. We report here on the optimization of oxygen transfer rates in deep-well microtiter plates and the development of a replication system allowing the simultaneous and reproducible sampling of 96 frozen glycerol stock cultures while the remaining culture volume remains frozen. Oxygen transfer rates were derived from growth curves of Pseudomonas putida and from rates of oxygen disappearance due to the cobalt-catalyzed oxidation of sulfite. Maximum oxygen transfer rates (38 mmol liter(-1) h(-1), corresponding to a mass transfer coefficient of 188 h(-1)) were measured during orbital shaking at 300 rpm at a shaking diameter of 5 cm and a culture volume of 0.5 ml. A shaking diameter of 2.5 cm resulted in threefold-lower values. These high oxygen transfer rates allowed P. putida to reach a cell density of approximately 9 g (dry weight) liter(-1) during growth on a glucose mineral medium at culture volumes of up to 1 ml. The growth-and-replication system was evaluated for a culture collection consisting of aerobic strains, mainly from the genera Pseudomonas, Rhodococcus, and Alcaligenes, using mineral media and rich media. Cross-contamination and excessive evaporation during vigorous aeration were adequately prevented by the use of a sandwich cover of spongy silicone and cotton wool on top of the microtiter plates.

Bacteriological Techniques↗
PubMed2000

Accumulation of Poly[(R)-3-hydroxyalkanoates] in Pseudomonas oleovorans during growth with octanoate in continuous culture at different dilution rates.

Pseudomonas oleovorans ATCC 29347 was grown in chemostat culture at different dilution rates with mineral media varying in their ratios of octanoate to ammonia (C(0)/N(0) ratio). At all dilution rates tested, three distinct growth regimes were observed: (i) carbon limitation with NH(4)(+) in excess at low C(0)/N(0) ratios, (ii) purely nitrogen-limited growth conditions at high C(0)/N(0) ratios with residual octanoate in the culture supernatant, and (iii) an intermediate zone of dual-nutrient-limited growth conditions where both the concentration of octanoate and that of ammonia were very low. The dual-nutrient-limited growth zone shifted to higher C(0)/N(0) ratios with decreasing dilution rates, and the extension of the dual-nutrient-limited growth zone was inversely proportional to the growth rate. The cells accumulated the storage compound medium-chain-length poly[(R)-3-hydroxyalkanoate] (mcl-PHA) during dual (C and N)-nutrient-limited and N-limited growth conditions. Within the dual-nutrient-limited growth zone, the cellular mcl-PHA contents increased when the C(0)/N(0) ratio in the feed was increased, whereas the cellular mcl-PHA level was independent from the feed C(0)/N(0) ratio during N-limited growth. The monomeric composition of the accumulated mcl-PHA was independent of both the dilution rate and the feed C(0)/N(0) ratio and consisted of 12 mol% 3-hydroxyhexanoic acid and 88 mol% 3-hydroxyoctanoic acid. Accumulation of mcl-PHA led to an increase in the cellular C/N ratio and to changes in elemental growth yields for nitrogen and carbon.

Caprylates↗
PubMed2000

Role of phaD in accumulation of medium-chain-length Poly(3-hydroxyalkanoates) in Pseudomonas oleovorans.

Pseudomonas oleovorans is capable of producing poly(3-hydroxyalkanoates) (PHAs) as intracellular storage material. To analyze the possible involvement of phaD in medium-chain-length (MCL) PHA biosynthesis, we generated a phaD knockout mutant by homologous recombination. Upon disruption of the phaD gene, MCL PHA polymer accumulation was decreased. The PHA granule size was reduced, and the number of granules inside the cell was increased. Furthermore, mutant cells appeared to be smaller than wild-type cells. Investigation of MCL PHA granules revealed that the pattern of granule-associated proteins was changed and that the predominant protein PhaI was missing in the mutant. Complementation of the mutant with a phaD-harboring plasmid partially restored the wild-type characteristics of MCL PHA production and fully restored the granule and cell sizes. Furthermore, PhaI was attached to the granules of the complemented mutant. These results indicate that the phaD gene encodes a protein which plays an important role in MCL PHA biosynthesis. However, although its main effect seems to be the stabilization of MCL PHA granules, we found that the PhaD protein is not a major granule-associated protein and therefore might act by an unknown mechanism involving the PhaI protein.

Amino Acid Sequence↗
PubMed2000

FabG, an NADPH-dependent 3-ketoacyl reductase of Pseudomonas aeruginosa, provides precursors for medium-chain-length poly-3-hydroxyalkanoate biosynthesis in Escherichia coli.

Escherichia coli hosts expressing fabG of Pseudomonas aeruginosa showed 3-ketoacyl coenzyme A (CoA) reductase activity toward R-3-hydroxyoctanoyl-CoA. Furthermore, E. coli recombinants carrying the poly-3-hydroxyalkanoate (PHA) polymerase-encoding gene phaC in addition to fabG accumulated medium-chain-length PHAs (mcl-PHAs) from alkanoates. When E. coli fadB or fadA mutants, which are deficient in steps downstream or upstream of the 3-ketoacyl-CoA formation step during beta-oxidation, respectively, were transformed with fabG, higher levels of PHA were synthesized in E. coli fadA, whereas similar levels of PHA were found in E. coli fadB, compared with those of the corresponding mutants carrying phaC alone. These results strongly suggest that FabG of P. aeruginosa is able to reduce mcl-3-ketoacyl-CoAs generated by the beta-oxidation to 3-hydroxyacyl-CoAs to provide precursors for the PHA polymerase.

3-Hydroxyacyl CoA Dehydrogenases↗
PubMed1999

Closed-loop control of bacterial high-cell-density fed-batch cultures: production of mcl-PHAs by Pseudomonas putida KT2442 under single-substrate and cofeeding conditions.

Pseudomonas putida KT2442 is able to accumulate medium-chain-length poly(3-hydroxyalkanoates) (mcl-PHAs) as intracellular inclusions on a variety of fatty acids and many other carbon sources. Some of these substrates, such as octanoic acid, alkenoic acids, and halogenated derivatives, are toxic when present in excess. Efficient production of mcl-PHAs on such toxic substrates therefore requires control of the carbon source concentration in the supernatant. In this study, we develop a closed-loop control system based on on-line gas chromatography to maintain continuously fed substrates at desired levels. We used the graphical programming environment LABVIEW to set up a flexible process control system that allows users to perform supervisory process control and permits remote access to the fermentation system over the Internet. Single-substrate supernatant concentration in a high-cell-density fed-batch fermentation process was controlled by a proportional (P) controller (P = 50%) acting on the substrate pump feed rate. Na-octanoate concentrations oscillated around the setpoint of 10 mM and could be maintained between 0 and 25 mM at substrate uptake rates as high as 90 mmol L(-1) h(-1). Under cofeeding conditions Na-10-undecenoate and Na-octanoate could be individually controlled at 2.5 mM and 9 mM, respectively, by applying a proportional integral (PI) controller for each substrate. The resulting copolymer contained 43.5 mol% unsaturated monomers and reflected the ratio of 10-undecenoate in the feed. It was suggested that both substrates were consumed at similar rates. These results show that this control system is suitable for avoiding substrate toxicity and supplying carbon substrates for growth and mcl-PHA accumulation.

Carbon↗
PubMed1999

Integrated two-liquid phase bioconversion and product-recovery processes for the oxidation of alkanes: process design and economic evaluation

Pseudomonas oleovorans and recombinant strains containing the alkane oxidation genes can produce alkane oxidation products in two-liquid phase bioreactor systems. In these bioprocesses the cells, which grow in the aqueous phase, oxidize apolar, non-water soluble substrates. The apolar products typically accumulate in the emulsified apolar phase. We have studied both the bioconversion systems and several downstream processing systems to separate and purify alkanols from these two-liquid phase media. Based on the information generated in these studies, we have now designed bioconversion and downstream processing systems for the production of 1-alkanols from n-alkanes on a 10 kiloton/yr scale, taking the conversion of n-octane to 1-octanol as a model system. Here, we describe overall designs of fed-batch and continuous-fermentation processes for the oxidation of octane to 1-octanol by Pseudomonas oleovorans, and we discuss the economics of these processes. In both systems the two-liquid phase system consists of an apolar phase with hexadecene as the apolar carrier solvent into which n-octane is dissolved, while the cells are present in the aqueous phase. In one system, multiple-batch fermentations are followed by continuous processing of the product from the separated apolar phase. The second system is based on alkane oxidation by continuously growing cultures, again followed by continuous processing of the product. Fewer fermentors were required and a higher space-time-yield was possible for production of 1-octanol in a continuous process. The overall performance of each of these two systems has been modeled with Aspen software. Investment and operating costs were estimated with input from equipment manufacturers and bulk-material suppliers. Based on this study, the production cost of 1-octanol is about 7 US$kg-1 when produced in the fed-batch process, and 8 US$kg-1 when produced continuously. The comparison of upstream and downstream capital costs and production costs showed significantly higher upstream costs for the fed-batch process and slightly higher upstream costs for continuous fermentation. The largest cost contribution was due to variable production costs, mainly resulting from media costs. The organisms used in these systems are P. putida alk+ recombinants which oxidize alkanes, but cannot oxidize the resulting alkanols further. Hence, such cells need a second carbon source, which in these systems is glucose. Although the continuous process is about 10% more expensive than the fed-batch process, improvements to reduce overall cost can be achieved more easily for continuous than for fed-batch fermentation by decreasing the dilution rate while maintaining near constant productivity. Improvements relevant to both processes can be achieved by increasing the biocatalyst performance, which results in improved overall efficiency, decreased capital investment, and hence, decreased production cost. Copyright 1999 John Wiley & Sons, Inc.

Journal Article↗
PubMed1999

Controlled regioselectivity of fatty acid oxidation by whole cells producing cytochrome P450BM-3 monooxygenase under varied dissolved oxygen concentrations.

Utilising whole cells of recombinant Escherichia coli K27 (pCYP102, pGEc47) containing active cytochrome P450BM-3 monooxygenase [E.C. 1. 14.14.1], multiple oxidations of saturated and unsaturated fatty acids were performed by the enzyme under conditions of excess oxygen. The amount of oxygen dissolved in the culture medium strongly influenced the regioselectivity of the reaction, as reflected in the distribution and amount of oxidised products. We have verified by gas chromatography/mass spectrometry that the products of in vivo biotransformation of pentadecanoic acid by cytochrome P450BM-3 are identical to those formed in cell-free extracts containing the enzyme. The formation of keto- and dihydroxy acids, side products which are characteristic for in vitro conversions with purified cytochrome P450BM-3 in the presence of excess oxygen, has been observed as well. Thus, by varying the oxygen concentration, we could control the regioselectivity of oxidation and the number of products made. Under oxygen limiting conditions, only monooxidised 12-, 13-, and 14-hydroxy-pentadecanoic acids were obtained. Consequently, unwanted side products could be excluded by modulating the amount of oxygen used in the bioconversion. Furthermore, whole cell oxidation of two unsaturated long-chain fatty acids, cis-pentadec-10-enoic and cis-hexadec-9-enoic acid, resulted in the production of epoxides, various subterminal hydroxyalkenoic acids and keto- and hydroxyalkanoic acids. Although we obtained higher activities of C15:0 conversion in vitro, the whole cell biocatalyst proved to be useful for specific oxidations of long-chain fatty acids since there is no need to add the costly cofactor NADPH. This biooxidation by E. coli K27 (pCYP102, pGEc47) under oxygen limitation has been demonstrated at the 2-L scale, showing that 12-, 13-, and 14-hydroxypentadecanoic acids can be produced in the g L-1 range.

Cytochrome P-450 Enzyme System↗
PubMed1999

An integrated process for the production of toxic catechols from toxic phenols based on a designer biocatalyst.

We describe the biocatalytic production of 3-phenylcatechol from 2-phenylphenol with the whole cell biocatalyst Escherichia coli JM101 (pHBP461). The recombinant produces 2-hydroxybiphenyl 3-monooxygenase, an enzyme from Pseudomonas azelaica HBP1. This enzyme introduces a hydroxyl-group at the C3-position of a variety of 2-substituted phenols, such as 2-phenylphenol. This permits the biocatalytic production of 3-substituted catechols, which are difficult to synthesize chemically. Both 2-phenylphenol and 3-phenylcatechol are highly toxic to E. coli. The toxic effects of 2-phenylphenol were minimized by feeding this substrate to the reactor at a rate slightly below the maximum biooxidation rate. As a result, the substrate concentration in the reactor remained below toxic levels during the bioconversion. The toxic product formed was removed by continuous adsorption on the solid resin Amberlite XAD-4. To this end the reaction mixture, containing the biocatalyst, was pumped continuously through an external loop with a fluidized bed of the resin. This resin efficiently and quantitatively adsorbed both 3-phenylcatechol and the remaining trace amounts of 2-phenylphenol. Consequently, the concentrations of these compounds were kept at subtoxic levels (below 100 mg L-1) and gram amounts of 3-phenylcatechol were produced with space-time yields of up to 0.39 g L-1 h-1. The product was recovered from the resin by acidic methanol elution and purified by recrystallization from n-hexane resulting in overall yields exceeding 59%. The optimized system served as a surprisingly simple and efficient integrated process, that allows the bioconversion of toxic substrates to toxic products with whole cell biocatalysts.

Adsorption↗
PubMed1999

Perspectives of medium chain length poly(hydroxyalkanoates), a versatile set of bacterial bioplastics

Medium chain length (mcl) poly(hydroxyalkanoic acids) (PHAs) are polyesters accumulated by fluorescent Pseudomonads and other bacteria. Work on the genetics of mcl-PHA formation has led to polymer synthesis in recombinant bacteria and plants. Several high and medium cost applications are now emerging. With optimized bacterial mcl-PHA synthesis on inexpensive agro-substrates and the development of plant-based mcl-PHAs in the next decade, the production economics of these bioplastics will ultimately permit their sustainable production for bulk applications.

Journal Article↗
PubMed1999

Molecular screening for alkane hydroxylase genes in Gram-negative and Gram-positive strains.

We have developed highly degenerate oligonucleotides for polymerase chain reaction (PCR) amplification of genes related to the Pseudomonas oleovorans GPo1 and Acinetobacter sp. ADP1 alkane hydroxylases, based on a number of highly conserved sequence motifs. In all Gram-negative and in two out of three Gram-positive strains able to grow on medium- (C6-C11) or long-chain n-alkanes (C12-C16), PCR products of the expected size were obtained. The PCR fragments were cloned and sequenced and found to encode peptides with 43.2-93.8% sequence identity to the corresponding fragment of the P. oleovorans GPo1 alkane hydroxylase. Strains that were unable to grow on n-alkanes did not yield PCR products with homology to alkane hydroxylase genes. The alkane hydroxylase genes of Acinetobacter calcoaceticus EB104 and Pseudomonas putida P1 were cloned using the PCR products as probes. The two genes allow an alkane hydroxylase-negative mutant of Acinetobacter sp. ADP1 and an Escherichia coli recombinant containing all P. oleovorans alk genes except alkB, respectively, to grow on n-alkanes, showing that the cloned genes do indeed encode alkane hydroxylases.

Acinetobacter calcoaceticus↗
PubMed1999

Engineering of a stable whole-cell biocatalyst capable of (S)-styrene oxide formation for continuous two-liquid-phase applications.

Recombinant strains of Pseudomonas putida KT2440 carrying genetic expression cassettes with xylene oxygenase- and styrene monooxygenase-encoding genes on their chromosomes could be induced in shaking-flask experiments to specific activities that rivaled those of multicopy-plasmid-based Escherichia coli recombinants. Such strains maintained the introduced styrene oxidation activity in continuous two-liquid-phase cultures for at least 100 generations, although at a lower level than in the shaking-flask experiments. The data suggest that placement of target genes on the chromosome might be a suitable route for the construction of segregationally stable and highly active whole-cell biocatalysts.

Bacteriological Techniques↗
PubMed1999

Production of medium-chain-length poly(3-hydroxyalkanoates) from gluconate by recombinant Escherichia coli.

It was shown recently that recombinant Escherichia coli, defective in the beta-oxidation cycle and harboring a medium-chain-length (MCL) poly(3-hydroxyalkanoate) (PHA) polymerase-encoding gene of Pseudomonas, is able to produce MCL PHA from fatty acids but not from sugars or gluconate (S. Langenbach, B. H. A. Rehm, and A. Steinbüchel, FEMS Microbiol. Lett. 150:303-309, 1997; Q. Ren, Ph.D. thesis, ETH Zürich, Zürich, Switzerland, 1997). In this study, we report the formation of MCL PHA from gluconate by recombinant E. coli. By introduction of genes coding for an MCL PHA polymerase and the cytosolic thioesterase I ('thioesterase I) into E. coli JMU193, we were able to engineer a pathway for the synthesis of MCL PHA from gluconate. We used two expression systems, i.e., the bad promoter and alk promoter, for the 'thioesterase I- and PHA polymerase-encoding genes, respectively, which enabled us to modulate their expression independently over a range of inducer concentrations, which resulted in a maximum MCL PHA accumulation of 2.3% of cell dry weight from gluconate. We found that the amount of PHA and the 'thioesterase I activity are directly correlated. Moreover, the polymer accumulated in the recombinant E. coli consisted mainly of 3-hydroxyoctanoate monomers. On the basis of our data, we propose an MCL PHA biosynthesis pathway scheme for recombinant E. coli JMU193, harboring PHA polymerase and 'thioesterase I, when grown on gluconate, which involves both de novo fatty acid synthesis and beta-oxidation.

Acyltransferases↗
PubMed1999

An alkane-responsive expression system for the production of fine chemicals

Membrane-located monooxygenase systems, such as the Pseudomonas putida mt-2-derived xylene oxygenase, are attractive for challenging transformations of apolar compounds, including enantiospecific epoxidations, but are difficult to synthesize at levels that are useful for application to biotechnological processes. In order to construct efficient biocatalysis strains, we utilized the alkane-responsive regulatory system of the OCT plasmid-located alk genes of Pseudomonas oleovorans GPo1, a very attractive system for recombinant biotransformation processes. Determination of the nucleotide sequence of alkS, whose activated gene product positively regulates the transcription of the structural genes alkBFGHJKL, on a 3.7-kb SalI-HpaI OCT plasmid fragment was completed, and the N-terminal amino acid sequence of an AlkS-LacZ fusion protein was found to be consistent with the predicted DNA sequence. The alkS gene and the alkBp promoter were assembled into a convenient alkane-responsive genetic expression cassette which allowed expression of the xylene oxygenase genes in a recombinant Escherichia coli strain at a specific activity of 91 U per g (dry weight) of cells when styrene was the substrate. This biocatalyst was used to produce (S)-styrene oxide in two-liquid-phase cultures. Volumetric productivities of more than 2 g of styrene oxide per h per liter of aqueous phase were obtained; these values represented a fivefold improvement compared with previous results.

Journal Article↗