Biomedical subjects

B Witholt

Publications and source records attributed to B Witholt.

At least 55 records · Page 3Linked to original sources

PubMed1999

Engineering of stable recombinant bacteria for production of chiral medium-chain-length poly-3-hydroxyalkanoates.

In order to scale up medium-chain-length polyhydroxyalkanoate (mcl-PHA) production in recombinant microorganisms, we generated and investigated different recombinant bacteria containing a stable regulated expression system for phaC1, which encodes one of the mcl-PHA polymerases of Pseudomonas oleovorans. We used the mini-Tn5 system as a tool to construct Escherichia coli 193MC1 and P. oleovorans POMC1, which had stable antibiotic resistance and PHA production phenotypes when they were cultured in a bioreactor in the absence of antibiotic selection. The molecular weight and the polydispersity index of the polymer varied, depending on the inducer level. E. coli 193MC1 produced considerably shorter polyesters than P. oleovorans produced; the weight average molecular weight ranged from 67,000 to 70,000, and the polydispersity index was 2.7. Lower amounts of inducer added to the media shifted the molecular weight to a higher value and resulted in a broader molecular mass distribution. In addition, we found that E. coli 193MC1 incorporated exclusively the R configuration of the 3-hydroxyoctanoate monomer into the polymer, which corroborated the enantioselectivity of the PhaC1 polymerase enzyme.

Acyltransferases↗

PubMed1999

Isolation and characterization of the cis-trans-unsaturated fatty acid isomerase of Pseudomonas oleovorans GPo12.

Pseudomonas oleovorans contains an isomerase which catalyzes the cis-trans conversion of the abundant unsaturated membrane fatty acids 9-cis-hexadecenoic acid (palmitoleic acid) and 11-cis-octadecenoic acid (vaccenic acid). We purified the isomerase from the periplasmic fraction of Pseudomonas oleovorans. The molecular mass of the enzyme was estimated to be 80 kDa under denaturing conditions and 70 kDa under native conditions, suggesting a monomeric structure of the active enzyme. N-terminal sequencing showed that the isomerase derives from a precursor with a signal sequence which is cleaved from the primary translation product in accord with the periplasmic localization of the enzyme. The purified isomerase acted only on free unsaturated fatty acids and not on esterified fatty acids. In contrast to the in vivo cis-trans conversion of lipids, this in vitro isomerization of free fatty acids did not require the addition of organic solvents. Pure phospholipids, even in the presence of organic solvents, could not serve as substrate for the isomerase. However, when crude membranes from Pseudomonas or Escherichia coli cells were used as phospholipid sources, a cis-trans isomerization was detectable which occurred only in the presence of organic solvents. These results indicate that isolated membranes from Pseudomonas or E. coli cells must contain factors which, activated by the addition of organic solvents, enable and control the cis-trans conversion of unsaturated acyl chains of membrane phospholipids by the periplasmic isomerase.

Alcohols↗

PubMed1999

PhaF, a polyhydroxyalkanoate-granule-associated protein of Pseudomonas oleovorans GPo1 involved in the regulatory expression system for pha genes.

The phaC1 gene codes for the medium-chain-length polyhydroxyalkanoate (mcl PHA) synthase of Pseudomonas oleovorans GPo1, which produces mcl PHA when grown in an excess of carbon source and under nitrogen limitation. In this work, we have demonstrated, by constructing a recombinant P. oleovorans strain carrying a phaC1::lacZ reporter system, that the phaC1 gene is expressed efficiently in the presence of octanoic acid while its expression is repressed when glucose or citrate is used as the carbon source. Moreover, a P. oleovorans GPo1 mutant (strain GPG-Tc6) expressing higher levels of the reporter gene than the wild-type strain in the presence of glucose or citrate has been generated by mini-Tn5 insertional mutagenesis. Characterization of this mutant allowed us to conclude that phaF, a gene located downstream of the pha gene cluster, was knocked out in this strain. P. oleovorans GPG-Tc6 regained the ability to control phaC1 gene expression when complemented with the phaF wild-type gene. Sequencing data revealed the presence of three complete open reading frames (ORFs) in this region: ORF1 and phaI and phaF genes. The amino acid sequences of the phaI gene product and the N-terminal half of the PhaF protein showed a significant degree of similarity. Furthermore, the primary structure of the PhaF C terminus identifies this protein as a member of the histone H1-like group of proteins. Northern blot analysis showed two transcription units containing phaF, i.e., phaF and phaIF transcripts. Expression of the phaIF operon is more efficient in the presence of octanoic acid and is enhanced by the lack of the PhaF protein. In addition, it has also been demonstrated that both PhaF and PhaI proteins are bound to PHA granules produced by P. oleovorans. A model for the role of PhaF in regulating PHA synthesis is presented.

Acyltransferases↗

PubMed1999

The PalkBFGHJKL promoter is under carbon catabolite repression control in Pseudomonas oleovorans but not in Escherichia coli alk+ recombinants.

The alk genes are located on the OCT plasmid of Pseudomonas oleovorans and encode an inducible pathway for the utilization of n-alkanes as carbon and energy sources. We have investigated the influence of alternative carbon sources on the induction of this pathway in P. oleovorans and Escherichia coli alk+ recombinants. In doing so, we confirmed earlier reports that induction of alkane hydroxylase activity in pseudomonads is subject to carbon catabolite repression. Specifically, synthesis of the monooxygenase component AlkB is repressed at the transcriptional level. The alk genes have been cloned into plasmid pGEc47, which has a copy number of about 5 to 10 per cell in both E. coli and pseudomonads. Pseudomonas putida GPo12 is a P. oleovorans derivative cured of the OCT plasmid. Upon introduction of pGEc47 in this strain, carbon catabolite repression of alkane hydroxylase activity was reduced significantly. In cultures of recombinant E. coli HB101 and W3110 carrying pGEc47, induction of AlkB and transcription of the alkB gene were no longer subject to carbon catabolite repression. This suggests that carbon catabolite repression of alkane degradation is regulated differently in Pseudomonas and in E. coli strains. These results also indicate that PalkBFGHJKL, the Palk promoter, might be useful in attaining high expression levels of heterologous genes in E. coli grown on inexpensive carbon sources which normally trigger carbon catabolite repression of native expression systems in this host.

Alkanes↗

PubMed1998

Medium chain length alkane solvent-cell transfer rates in two-liquid phase, pseudomonas oleovorans cultures

The oxidation of medium chain length alkanes and alkenes (C6 to C12) by Pseudomonas oleovorans and related, biocatalytically active recombinant organisms, in two-liquid phase cultures can be used for the biochemical production of several interesting fine chemicals. The volumetric productivities that can be attained in two-liquid phase systems can be, in contrast to aqueous fermentations, limited by the transport of substrates from an apolar phase to the cells residing in the aqueous phase and by toxic effects of apolar solvents on microbial cells. We have assessed the impact of these possible limitations on attainable productivities in two-liquid phase fermentations operated with mcl-alkanes. Pseudomonas oleovorans grows well in two-liquid phase media containing a bulk n-octane phase as the sole carbon source. However, cells are also damaged, typically resulting in a cell lysis rate of about 0.08 to 0. 10 h-1. These rates could be lowered by 50 to 70% to 0.03 h-1 and substrate yields increased from 0.55 to 0.85 g g-1 by diluting octane in non-metabolizable long-chain hydrocarbon solvents. Transfer rates of medium chain length (mcl) alkanes from the apolar phase to the cells were determined by following growth and the rate at which carbon-containing metabolites accumulated in the different phases of the cultures. mcl-Alkane solvent-cell transfer rates of at least 79, 64, and 18 mmol per liter of aqueous medium per hour were determined for n-heptane, n-octane, and n-decane, respectively. Rates of up to 30 mmol L-1 h-1 were observed under octane-limiting conditions in systems where the apolar substrate was dissolved to concentrations below 3% (v/v) in hexadecene. Based on low power input experiments, we estimated the maximum obtainable mass transfer rates in large scale processes to be in the range of 13 mmol L-1 h-1 for decane and higher than 45 mmol L-1 h-1 for octane and heptane. The results indicate that high solvent to cell mass transfer rates and minimized cell damage will enable high production rates in two-liquid phase bioprocesses, justifying ongoing efforts to attain high densities of catalytically, highly active cells in such systems. Copyright 1998 John Wiley & Sons, Inc.

Journal Article↗

PubMed1998

Biotransformation of octane by E. coli HB101[pGEc47] on defined medium: octanoate production and product inhibition.

E. coli HB101[pGEc47], which is able to convert octane to octanoate, but cannot oxidize octanoate further, was grown on defined medium with glucose as carbon source in batch and continuous culture. The biomass yield on glucose decreased from 0.32 +/- 0.02 g g-1 in aqueous cultivations to 0.25 +/- 0.02 g g-1 in the presence of octane. Maximal octanoate productivities of 0.6 g L-1 h-1 were the same as found in cultivations on complex medium. The glucose-based carbon recovery in these experiments was 99 +/- 4% (in extreme, between 90% and 105%). An increase of the octane feed from 1% to 2% (v/v) or more led to washout of cells. This effect was reversible when the octane feed was decreased to its initial value of 1%. Analysis of experimental data by model simulation strongly suggested that washout was due to inhibition by octanoate only. Pulses of octanoate to a continuous culture grown on aqueous media were applied to analyze the inhibition further. Inhibition by acetate was not significant, but its presence in the medium reflected a physiological state that made the cells more sensitive to octanoate inhibition. Model simulation with linear inhibition kinetics could perfectly predict glucose consumption and the resulting glucose concentration. The linear type of inhibition was confirmed by a variety of batch experiments in the presence of different concentrations of octanoate. The glucose-based specific growth rate, mu, decreased linearly with increasing concentrations of octanoate and became zero at a threshold concentration pmax of 5.25 +/- 0.25 g L-1.

Bioreactors↗

PubMed1998

Growth characteristics of Escherichia coli HB101[pGEc47] on defined medium.

This paper shows that differences in growth behavior of Escherichia coli strain HB101 and strain HB101[pGEc47] can be related to yeast extract-enriched medium rather than plasmid properties. An optimal medium for growth of E. coli HB101[pGEc47] was designed based on the individual yield coefficients for specific medium components (NH4+ 6 g g-1, PO43- 14 g g-1, SO42- 50 g g-1). The yield coefficient for L-leucine depends on the glucose content of the medium (20 g g-1 for 3% glucose, 40 g g-1 for 1% glucose) and the yield coefficient for L-proline depends on the cultivation mode (20 g g-1 for batch cultivation, 44 g g-1 for continuous cultivation). Growth on defined medium after medium optimization is as rapid as on complex medium (0. 42-0.45 h-1). The critical dilution rate (DR) in the defined medium above which undesired production of acetic acid occurs is in the range of 0.23-0.26 h-1.

Bacteriological Techniques↗

PubMed1998

Synthesis of alkane hydroxylase of Pseudomonas oleovorans increases the iron requirement of alk+ bacterial strains.

The alk genes enable Pseudomonas oleovorans to utilize alkanes as sole carbon and energy source. Expression of the alk genes in P. oleovorans and in two Escherichia coli recombinants induced iron limitation in minimal medium cultures. Further investigation showed that the expression of the alkB gene, encoding the integral cytoplasmic membrane protein AlkB, was responsible for the increase of the iron requirement of E. coli W3110 (pGEc47). AlkB is the non-heme iron monooxygenase component of the alkane hydroxylase system, and can be synthesized to levels up to 10% (w/w) of total cell protein in E. coli W3110 (pGEc47). Its synthesis is, however, strictly dependent on the presence of sufficient iron in the medium. Our results show that a glucose-grown E. coli alk+ strain can reach alkane hydroxylase activities of about 25 U/g cdw, and are consistent with the recent finding that catalytically active AlkB contains two, rather than one iron atom per polypeptide chain.

Biotechnology↗

PubMed1998

Developments toward large-scale bacterial bioprocesses in the presence of bulk amounts of organic solvents.

Many pseudomonads and other bacteria can grow on aliphatic and aromatic hydrocarbons that occur in the environment. We are examining the potential of such organisms as biocatalysts for the oxidation of a variety of substituted aliphatic and aromatic compounds. To attain a high production rate of oxidation products via such biotransformations, we have focused on two-liquid phase culture systems. In these systems, cells are grown in liquid media consisting of an aqueous phase containing water-soluble growth substrates and droplets of a water-immicible organic solvent containing bioconversion substrates and products. For industrial applications of such two-liquid phase processes, several questions remain. What are the maximum rates at which apolar compounds can be transferred from the apolar phase to cells growing in the aqueous phase, i.e., what are the maximum space-time yields attainable in two-liquid phase fermentations under practical conditions? What does an efficient downstream processing of two-liquid phase medium involve? What safety regimes should be considered in working with flammable organic solvents? Can elevated pressure be used to increase oxygen transfer? Based on answers to these questions, we have recently developed a high-pressure, explosion-proof bioreactor system with Bioengineering AG (Wald, Switzerland), which will be installed in our pilot plant and used to explore two-liquid phase bioconversions at a pilot scale.

Bacteria↗

PubMed1998

Biocatalyst engineering by assembly of fatty acid transport and oxidation activities for In vivo application of cytochrome P-450BM-3 monooxygenase.

The application of whole cells containing cytochrome P-450BM-3 monooxygenase [EC 1.14.14.1] for the bioconversion of long-chain saturated fatty acids to omega-1, omega-2, and omega-3 hydroxy fatty acids was investigated. We utilized pentadecanoic acid and studied its conversion to a mixture of 12-, 13-, and 14-hydroxypentadecanoic acids by this monooxygenase. For this purpose, Escherichia coli recombinants containing plasmid pCYP102 producing the fatty acid monooxygenase cytochrome P-450BM-3 were used. To overcome inefficient uptake of pentadecanoic acid by intact E. coli cells, we made use of a cloned fatty acid uptake system from Pseudomonas oleovorans which, in contrast to the common FadL fatty acid uptake system of E. coli, does not require coupling by FadD (acyl-coenzyme A synthetase) of the imported fatty acid to coenzyme A. This system from P. oleovorans is encoded by a gene carried by plasmid pGEc47, which has been shown to effect facilitated uptake of oleic acid in E. coli W3110 (M. Nieboer, Ph.D. thesis, University of Groningen, Groningen, The Netherlands, 1996). By using a double recombinant of E. coli K27, which is a fadD mutant and therefore unable to consume substrates or products via the beta-oxidation cycle, a twofold increase in productivity was achieved. Applying cytochrome P-450BM-3 monooxygenase as a biocatalyst in whole cells does not require the exogenous addition of the costly cofactor NADPH. In combination with the coenzyme A-independent fatty acid uptake system from P. oleovorans, cytochrome P-450BM-3 recombinants appear to be useful alternatives to the enzymatic approach for the bioconversion of long-chain fatty acids to subterminal hydroxylated fatty acids.

Bacterial Proteins↗

PubMed1998

Towards a biocatalyst for (S)-styrene oxide production: characterization of the styrene degradation pathway of Pseudomonas sp. strain VLB120.

In order to design a biocatalyst for the production of optically pure styrene oxide, an important building block in organic synthesis, the metabolic pathway and molecular biology of styrene degradation in Pseudomonas sp. strain VLB120 was investigated. A 5.7-kb XhoI fragment, which contained on the same strand of DNA six genes involved in styrene degradation, was isolated from a gene library of this organism in Escherichia coli by screening for indigo formation. T7 RNA polymerase expression experiments indicated that this fragment coded for at least five complete polypeptides, StyRABCD, corresponding to five of the six genes. The first two genes encoded the potential carboxy-terminal part of a sensor, named StySc, and the complete response regulator StyR. Fusion of the putative styAp promoter to a lacZ reporter indicated that StySc and StyR together regulate expression of the structural genes at the transcriptional level. Expression of styScR also alleviated a block that prevented translation of styA mRNA when a heterologous promoter was used. The structural genes styA and styB produced a styrene monooxygenase that converted styrene to styrene oxide, which was then converted to phenylacetaldehyde by StyC. Sequence homology analysis of StyD indicated a probable function as a phenylacetaldehyde dehydrogenase. To assess the usefulness of the enzymes for the production of enantiomerically pure styrene oxide, we investigated the enantiospecificities of the reactions involved. Kinetic resolution of racemic styrene oxide by styrene oxide isomerase was studied with E. coli recombinants carrying styC, which converted styrene oxide at a very high rate but with only a slight preference for the S enantiomer. However, recombinants producing styrene monooxygenase catalyzed the formation of (S)-styrene oxide from inexpensive styrene with an excellent enantiomeric excess of more than 99% at rates up to 180 U g (dry weight) of cells-1.

Base Sequence↗

PubMed1997

In vitro activities of granule-bound poly[(R)-3-hydroxyalkanoate]polymerase C1 of Pseudomonas oleovorans--development of an activity test for medium-chain-length-poly(3-hydroxyalkanoate) polymerases.

A newly developed in vitro activity assay for medium-chain-length (mcl)-poly(3-hydroxyalkanoate) polymerases is described. Polymerase C1 of Pseudomonas oleovorans GPo1 attached to isolated granules was used as model enzyme. A direct correlation was found between (R)-3-hydroxyoctanoylCoA depletion and poly(3-hydroxyalkanoate) synthesis due to polymerase C1 activity. Highest activities of 1.13 U/mg granule bound protein and highest specific activities of 2.3 U/mg polymerase C1 were determined towards (RS)-3-hydroxyoctanoylCoA. A first determination of a Km value for mcl poly(3-hydroxyalkanoate) polymerases was performed leading to an estimated Km of 0.16 (+/-0.1) mM for granule bound polymerase C1 with (R)-3-hydroxyoctanoylCoA as substrate. Polymerase C1 showed no activity towards (RS)-3-hydroxybutyrylCoA and a specific activity of 0.28 U/mg polymerase C1 for (R)-3-hydroxyvalerylCoA. (R)-3-HydroxyoctanoylCoA and a mixture of (RS)-3-hydroxyoctanoylCoA were both depleted for more than 75% by granule-bound polymerase C1, suggesting a non-rate-limiting epimerase activity attached to poly(3-hydroxyalkanoate) granules isolated from Pseudomonas putida GPp104[pGEc405]. Whereas no relationship was found between the activity of granule-bound polymerase C1 and poly(3-hydroxyalkanoate) content of the granules, higher activities were measured when a higher substrate concentration or more enzyme was present in the in vitro activity assay.

Acyltransferases↗

PubMed1997

The AlkB monooxygenase of Pseudomonas oleovorans--synthesis, stability and level in recombinant Escherichia coli and the native host.

We have studied the synthesis and stability of the monooxygenase AlkB of Pseudomonas oleovorans in its natural host and in recombinant Escherichia coli. Three strains were investigated: the prototype strain P. oleovorans and the E. coli alk+ recombinants HB101 (pGEc47) and W3110 (pGEc47). Plasmid pGEc47 allows regulated expression of alkB and synthesis of active AlkB in E. coli. The E. coli strains were selected because E. coli HB101 (pGEc47) produces similar amounts of AlkB as P. oleovorans (1.5-2% of total cell protein), whereas E. coli W3110 (pGEc47) is able to make substantially (about fivefold) more AlkB. The AlkB synthesis and degradation rates in batch cultures of the three strains were determined by means of isotopic-labeling and immunological techniques. The mean specific AlkB synthesis rates in P. oleovorans, E. coli HB101 (pGEc47) and E. coli W3110 (pGEc47) were approximately 7, 12.5 and 45 microg x mg protein(-1) x h(-1), respectively. The half-lives of AlkB were estimated to be 80, 3 and 15 for P. oleovorans, E. coli HB101 (pGEc47) and E. coli W3110 (pGEc47), respectively. Thus, the intracellular AlkB level in each of the three strains was the result of their AlkB synthesis and degradation rates. The AlkB level during batch growth was modelled by means of experimentally derived parameters for AlkB synthesis and degradation, and showed good agreement with AlkB levels determined by means of immunoblotting in all strains investigated.

Cytochrome P-450 CYP4A↗

PubMed1997

Polymerase C1 levels and poly(R-3-hydroxyalkanoate) synthesis in wild-type and recombinant Pseudomonas strains.

A functional antibody highly specific for polymerase C1 of Pseudomonas oleovorans GPo1 was raised and used to determine polymerase C1 levels in in vivo experiments. The polymerase C1 antibodies did not show a cross-reaction with polymerase C2 of P. oleovorans. In wild-type P. oleovorans GPo1 and Pseudomonas putida KT2442, amounts of 0.075 and 0.06% polymerase relative to total protein, respectively, were found. P. oleovorans GPo1(pGEc405), which contained additional copies of the polymerase C1-encoding gene under the control of its native promoter, contained 0.5% polymerase C1 relative to total protein. Polymerase C1 reached 10% of total cell protein when the polymerase C1-encoding gene was overexpressed through the P(alk) promoter in P. oleovorans GPo1(pET702, pGEc74). Amounts of poly(R-3-hydroxyalkanoate) (PHA) increased significantly under non-nitrogen-limiting conditions when additional polymerase C1 was expressed in P. oleovorans. Whereas P. oleovorans produced 34% (wt/wt) PHA under these conditions, a PHA level of 64% (wt/wt) could be reached for P. oleovorans GPo1(pGEc405) and a PHA level of 52% (wt/wt) could be reached for P. oleovorans GPo1(pET702, pGEc74) after induction, compared to a PHA level of 13% for the uninduced control. All recombinant Pseudomonas strains containing additional polymerase C1 showed small changes in their PHA composition. Larger amounts of 3-hydroxyhexanoate monomer and smaller amounts of 3-hydroxyoctanoate and -decanoate were found compared to those of the wild type. Two different methods were developed to quantify rates of incorporation of new monomers into preexisting PHA granules. P. oleovorans GPo1 cells grown under nitrogen-limiting conditions showed growth stage-dependent incorporation rates. The highest PHA synthesis rates of 9.5 nmol of C8/C6 monomers/mg of cell dry weight (CDW)/min were found during the mid-stationary phase, which equals a rate of production of 80 g of PHA/kg of CDW/h.

Acyltransferases↗

PubMed1997

Determinants for overproduction of the Pseudomonas oleovorans cytoplasmic membrane protein alkane hydroxylase in alk+ Escherichia coli W3110.

The Pseudomonas oleovorans alkB gene is expressed in alk+ Escherichia coli W3110 to 10 to 15% of the total cell protein, which is exceptional for a (foreign) cytoplasmic membrane protein. In other E. coli recombinants such as alk+ HB101, AlkB constitutes 2 to 3% of the total protein. In this study, we have investigated which factors determine the expression level of alkB in alk+ W3110. In particular, we have investigated the role of AlkB-induced stimulation of phospholipid synthesis. Blocking phospholipid synthesis in alk+ W3110 did not specifically alter the expression of alkB, and we conclude that stimulation of phospholipid synthesis is not a prerequisite for high-level expression of the membrane protein. W3110 is able to produce exceptionally high levels of alkane monooxygenase, because the rate of alkB mRNA synthesis in W3110 is an order of magnitude higher than that in HB101. This may be due in part to the higher copy number of pGEc47 in W3110 in comparison with HB101.

Bacterial Proteins↗

PubMed1996

Overproduction of a foreign membrane protein in Escherichia coli stimulates and depends on phospholipid synthesis.

When the Pseudomonas oleovorans alk system, consisting of the alkBFGHJKL and alkST genes, is expressed in Escherichia coli W3110, significant changes in phospholipid metabolism of the host are observed. A major role seems to be played by the cytoplasmic membrane protein alkane hydroxylase (AlkB), which is synthesized as up to 10-15% of the total protein in this strain [Nieboer, M., Kingma, J. & Witholt, B. (1993) The alkane oxidation system of Pseudomonas oleovorans: induction of the alk genes in Escherichia coli W3110[pGEc47] affects membrane biogenesis and results in overexpression of alkane hydroxylase in a distinct cytoplasmic membrane subfraction, Mol. Microbiol. 8, 1039-1051]. In the present paper, we have studied the link between synthesis of the membrane protein and the synthesis of phospholipids and fatty acids by examining the kinetics of these processes. Using [35S]methionine labeling, it was shown that induction of AlkB was maximal within 30-60 min after addition of inducer, when up to 15% of all newly synthesized protein is AlkB. Phospholipid synthesis was followed by measuring the incorporation of 14C-labeled acetate and 33P-labeled phosphoric acid into phospholipids. Despite a negative effect of the inducer on the growth rate of W3110[pGEc47], net phospholipid synthesis was significantly enhanced as a result of the expression of alkB. Synthesis of all three major phospholipids were stimulated to comparable extents by the induction of alkB. Induction did not increase 33P incorporation into lipids in the control recombinant alk+ strain which lacked alkB. Simultaneous with AlkB synthesis, the conversion of unsaturated 9-hexadecenoic acid (C16:1) into 9,10-methylene hexadecanoic acid (C17:ocyc) was reduced in the alk+ recombinant. Overall, these data show that the production of a foreign membrane protein in E. coli can engender a response of the phospholipid-synthesizing system of the host. In the absence of such a response, induction of the alk system would be much more toxic to the cells. Apparently, the increased phospholipid synthesis plays an important role in enabling the AlkB overproducing strain to grow.

Bacterial Proteins↗

PubMed1996

Physiological changes and alk gene instability in Pseudomonas oleovorans during induction and expression of alk genes.

The alk genes of Pseudomonas oleovorans, which is able to metabolize alkanes and alkenes, are organized in alkST and alkBFGHJKL clusters, in which the expression of alkBFGHJKL is positively regulated by AlkS. Growth of the wild-type strain GPo1 and P. oleovorans GPo12 alk recombinants on octane resulted in changes of cellular physiology and morphology. These changes, which included lower growth rates and a reduction of the number of CFU due to filamentation, were also seen when the cells were grown on aqueous medium, and the alk genes were induced with dicyclopropylketone, a gratuitous inducer of the alk genes. These effects were seen only for recombinants carrying both alkST and alkBFGHJKL operons. Deletion of parts of either alkB or alkJ, which encode two major Alk proteins located in the cytoplasmic membrane, modified but did not eliminate the effects described above, suggesting that they were due to induction and expression of several alk genes. Continuous growth of the cells in the presence of dicyclopropylketone for about 10 generations led to inactivation, but not elimination, of the alk genes. This resulted in a return of the recombinants to normal physiology and growth.

Alkanes↗

PubMed1995

Production of Pseudomonas aeruginosa Rhamnolipid Biosurfactants in Heterologous Hosts.

The high-level production of rhamnolipid biosurfactants is a unique feature of Pseudomonas aeruginosa and is strictly regulated in response to environmental conditions. The final step in rhamnolipid biosynthesis is catalyzed by the rhlAB genes encoding a rhamnosyltransferase. The expression of the cloned rhlAB genes was studied in heterologous hosts, either under the control of the rhlR and rhlI rhamnolipid regulatory elements or under the control of the tac promoter. A recombinant P. fluorescens strain harboring multiple plasmid-encoded copies of the rhamnolipid gene cluster produced rhamnolipids (0.25 g liter(sup-1)) when grown under nitrogen-limiting conditions. The highest yields (0.6 g liter(sup-1)) and productivities (24 mg liter(sup-1) h(sup-1)) were obtained in a recombinant Pseudomonas putida strain, KT2442, harboring promoterless rhlAB genes fused to the tac promoter on a plasmid. Active rhamnosyltransferase was synthesized, but no rhamnolipids were produced, by recombinant Escherichia coli upon induction of rhlAB gene expression.

Journal Article↗