Characterization of temperature-sensitive and lipopolysaccharide overproducing transposon mutants of Pseudomonas putida CA-3 affected in PHA accumulation

A library of 20 000 transposon (Tn5) mutants of the gram-negative bacterium Pseudomonas putida CA-3 was generated and screened for adverse affects in polyhydroxyalkanoates (PHA) accumulation. Two mutants of interest were characterized phenotypically. CA-3-126, a mutant disrupted in a stress-related protein Clp protease subunit ClpA, demonstrated greater decreases in PHA accumulation compared with the wild type at reduced and elevated temperatures under PHA-accumulating growth conditions. CA-3-M, which is affected in the aminotransferase class I enzyme, accumulated reduced levels of PHA relative to the wild type and had lower growth yields on all carbon sources tested. Mutant CA-3-M produced up to 10-fold higher levels of lipopolysaccharide relative to the wild type and exhibited 1.2-fold lower aminotransferase activity with phenylalanine as a substrate compared with the wild-type strain. The composition of the lipopolysaccharide produced by the mutant differed from that produced by the wild-type strain. Growth and PHA accumulation by CA-3-M was the same as the wild type when the nitrogen concentration in the medium was increased to 265 mg N L⁻¹.     

Growth and accumulation dynamics of poly(3-hydroxyalkanoate) (PHA) in Pseudomonas putida GPo1 cultivated in continuous culture under transient feed conditions

It has been shown that Pseudomonas putida GPo1 is able to grow in continuous culture simultaneously limited by ammonium (N source) and octanoate (C source), and concomitantly accumulate poly([R]-3-hydroxyalkanoate) (PHA). Under such growth conditions the material properties of PHA can be fine-tuned if a second PHA precursor substrate is supplied. To determine the range of dual carbon and nitrogen (C, N)-limited growth conditions, tedious chemostat experiments need to be carried out for each carbon source separately. To determine the growth regime, the C/N ratio of the feed (f) to a chemostat was changed in a stepwise manner at a constant dilution rate of 0.3/h. Dual-(C, N)-limited growth was observed between C(f) /N(f) ≤ 6.4 g/g and C(f) /N(f) >9.5 g/g. In the following, we analyzed alternative approaches, using continuous medium gradients at the same dilution rate, that do not require time consuming establishments of steady states. Different dynamic approaches were selected in which the C(f) /N(f) ratio was changed continuously through a convex increase of C(f) , a convex increase of N(f) , or a linear decrease of C(f) (gradients 1, 2, and 3, respectively). In these experiments, the dual-(C, N)-limited growth regime was between 7.2 and 11.0 g/g for gradient 1, 4.3 and 6.9 g/g for gradient 2, and 5.1 and 8.9 g/g for gradient 3. A mathematical equation was developed that compensated a time delay of the gradient that was caused by the wash-in/wash-out effects of the medium feed.     

The role of fatty acid biosynthesis and degradation in the supply of substrates for poly(3-hydroxyalkanoate) formation in Pseudomonas putida

Abstract The relationship between fatty acid metabolism and PHA biosynthesis in P. putida is described. Detailed ¹H and ¹³C NMR studies were performed to investigate the structures of poly(3-hydroxyalkanoates) (PHAs) formed from carbohydrates and fatty acids. On the basis of these results, it is proposed that during growth on glucose the 3-hydroxyacyl-acyl carrier protein intermediates of the de novo fatty acid biosynthetic pathway are diverted to PHA biosynthesis. Similarly, further evidence is presented that during cultivation on fatty acids, intermediates of the β-oxidation cycle serve as precursors of PHA biosynthesis.     

Production of Poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) from Gluconate and Glucose by Recombinant Aeromonas hydrophila and Pseudomonas putida

Aeromonas hydrophila 4AK4 and Pseudomonas putida GPp104 were genetically engineered to synthesize poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) using gluconate and glucose rather than fatty acids. A truncated tesA gene, encoding cytosolic thioesterase I of Escherichia coli which catalyzes the conversion of acyl-ACP into free fatty acids, was introduced into A. hydrophila 4AK4. When grown in gluconate, the recombinant A. hydrophila 4AK4 synthesized 10% (w/w) PHBHHx containing 14% (mol/mol) 3-hydroxyhexanoate. If additional PHBHHx synthesis genes, phaPCJ, were over-expressed with the truncated tesA in A. hydrophila 4AK4, the PHBHHx content increased to 15% (w/w) and contained 19% (mol/mol) 3-hydroxyhexanoate. Recombinant P. putida GPp104 harboring phaC encoding PHBHHx synthase of A. hydrophila, phaB encoding acetoacetyl-CoA reductase of Wautersia eutropha and phaG encoding 3-hydroxyacyl-ACP-CoA transferase of P. putida, synthesized 19% (w/w) PHBHHx containing 5% (mol/mol) 3-hydroxyhexanoate from glucose. The results suggest that the engineered pathways were applicable to synthesize PHBHHx from unrelated carbon sources such as gluconate and glucose.     

Exploiting metagenomic diversity for novel polyhydroxyalkanoate synthases: production of a terpolymer poly(3-hydroxybutyrate-co-3-hydroxyhexanoate-co-3-hydroxyoctanoate) with a recombinant Pseudomonas putida strain

A metagenomic library of 2.1 × 10⁶ clones was constructed using oil-contaminated soil from Gujarat (India). One of the fosmid clones, 40N22, encodes a polyhydroxyalkanoate synthase showing 76% identity with an Alcaligenes sp. synthase. The corresponding gene was expressed in Pseudomonas putida KT2440 ΔphaC1 which is impaired in PHA production. The gene conferred the recombinant strain PpKT-40N22 with the ability to produce copolymers with up to 21% in medium-chain-length content. Thus, 37% and 45% of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) and poly(3-hydroxybutyrate-co-3-hydroxyhexanoate-co-3-hydroxyoctanoate), respectively were obtained when using sodium heptanoate and oleic acid as carbon sources. These 3-hydroxybutyrate-(3HB)-based polymers are of interest since they incorporate the properties of medium chain length polymers and thus increase the range of applications of PHAs.     

Engineering Native and Synthetic Pathways in Pseudomonas putida for the Production of Tailored Polyhydroxyalkanoates

Growing environmental concern sparks renewed interest in the sustainable production of (bio)materials that can replace oil-derived goods. Polyhydroxyalkanoates (PHAs) are isotactic polymers that play a critical role in the central metabolism of producer bacteria, as they act as dynamic reservoirs of carbon and reducing equivalents. PHAs continue to attract industrial attention as a starting point toward renewable, biodegradable, biocompatible, and versatile thermoplastic and elastomeric materials. Pseudomonas species have been known for long as efficient biopolymer producers, especially for medium-chain-length PHAs. The surge of synthetic biology and metabolic engineering approaches in recent years offers the possibility of exploiting the untapped potential of Pseudomonas cell factories for the production of tailored PHAs. In this article, an overview of the metabolic and regulatory circuits that rule PHA accumulation in Pseudomonas putida is provided, and approaches leading to the biosynthesis of novel polymers (e.g., PHAs including nonbiological chemical elements in their structures) are discussed. The potential of novel PHAs to disrupt existing and future market segments is closer to realization than ever before. The review is concluded by pinpointing challenges that currently hinder the wide adoption of bio-based PHAs, and strategies toward programmable polymer biosynthesis from alternative substrates in engineered P. putida strains are proposed.     

Analysis of polyhydroxyalkanoate (PHA) synthase gene in activated sludge that produces PHA containing 3-hydroxy-2-methylvalerate

The identification of phaC which encodes PHA synthase, that is involved in the formation of polyhydroxyalkanoate (PHA) containing 3-hydroxy-2-methylvalerate (3H2MV), was attempted. As of now, PHA containing 3H2MV has been reported to be produced only by mixed microbial cultures in activated sludge, but no pure bacterial cultures. A laboratory-scale activated sludge process was operated for 67 days. During the operation of the activated sludge process, its capacity to produce PHA containing 3H2MV, and the diversity of the partial phaC genes in the activated sludge microorganisms were monitored periodically. Analysis of the partial phaC genes was conducted by PCR followed by cloning and DNA sequencing, or by PCR followed by terminal-restriction fragment length polymorphism (T-RFLP). The cloning-sequencing of the 263 clones gave 11 distinct genetic groups (GGs). All of the genetic groups had similarities to known phaC higher than 48%, and one of them had similarity as high as 96% to that of Alcaligenes sp. The behavior of each of the genetic groups during the operation of the activated sludge process was monitored by the T-RFLP method. The restriction enzyme AccII, with the help of MboI, enabled the monitoring of each of the genetic groups. One of the genetic groups was found to have a strong correlation with the capability of the activated sludge to produce PHA containing 3H2MV, and its DNA sequence together with its amino acid sequence are reported.     

中长链聚羟基脂肪酸酯（mcl PHA）在嗜水气单胞菌I型PHA合酶缺失突变株中的合成

拥有Ⅰ型聚羟基脂肪酸酯(PHA)合酶基因的嗜水气单胞菌CGMCC0911株可利用月桂酸而不能利用葡萄糖作为碳源积累PHBHHx。将氯霉素抗性基因(Cm)插入到该基因中,获得带有I型PHA合酶断裂基因(phaC::Cm)的自杀质粒pFH10。自杀质粒pFH10通过接合作用转入嗜水气单胞菌CGMCC0911株中并发生体内同源重组,Cm被整合到基因组上,获得Ⅰ型PHA合酶缺失突变株。DNA序列测定证明了这一结果。GC分析表明,突变株不再产生PHBHHx,但却可利用月桂酸或葡萄糖积累中长链PHA,明显表明野生型嗜水气单胞菌基因组中存在另一个编码Ⅱ型PHA合酶的基因,且只有Ⅰ型PHA合酶被钝化后,这个功能被隐藏的Ⅱ型PHA合酶才可在细胞中发挥作用。     

Optimization of cyanophycin production in recombinant strains of Pseudomonas putida and Ralstonia eutropha employing elementary mode analysis and statistical experimental design

Elementary mode analysis was applied to simulate conditions for cyanophycin (CGP) biosynthesis and to optimize its production in bacteria. The conclusions from these simulations were confirmed by experiments with recombinant strains of the wild types and polyhydroxyalkanoate (PHA)-negative mutants of Ralstonia eutropha and Pseudomonas putida expressing CGP synthetase genes (cphA) of Synechocystis sp. strain PCC6308 or Anabaena sp. strain PCC7120. In particular, the effects of suitable precursor substrates and of oxygen supply as well as of the capability to accumulate PHA in addition to CGP biosynthesis were investigated. Since CGP consists of the amino acids aspartate and arginine, the tricarboxylic acid cycle (TCC), which provides intermediates for biosynthesis of these amino acids, seems to be important. Excretion of intermediates of the TCC upon cultivation at restricted oxygen supply and conversion of fumarate mainly to malate and to only little succinate in the absence of oxygen indicated that TCC intermediates for arginine and aspartate biosynthesis were provided by the oxidative or reductive parts of the TCC, respectively. The following important conclusions were made from the experiments and the simulations: (i) external arginine additionally supplied to the medium, (ii) oxygen limitation, and (iii) absence of PHA accumulation exerted positive effects on CGP accumulation. These conclusions were utilized to obtain CGP contents in the cells of as high as 17.9% (w x w(-1)) during cultivation of the investigated bacteria at the 30-L scale using mineral salts medium. Such high CGP contents were previously not obtained with these bacteria at a 30-L scale, even if complex media were used.     

Production and characterization of a new bioemulsifier from Pseudomonas putida ML2

AIMS: To characterize the bioemulsifier produced by a nonfluorescent strain of Pseudomonas putida isolated from a polluted sediment and to determine the influence of pH, temperature, media composition, and carbon and nitrogen source on growth and emulsifying activity. METHODS AND RESULTS: Different indexes were employed to determine the emulsifying properties of culture supernatants of P. putida ML2 in defined and complex media. Surface tension of cell-free supernatants was measured. Purification and chemical analysis of the emulsifier was performed. Confirmed results indicate that a polysaccharide with hexasaccharide repeating units is responsible for the emulsifying activity in a mineral medium with glucose as sole carbon source. Moreover, an emulsifier is produced when growing on naphthalene. CONCLUSIONS: Culture media composition influences the amount and the properties of the emulsifier produced by this P. putida strain. Under nitrogen limiting conditions, a polysaccharide is responsible for the emulsifying activity in defined mineral media. In complex nitrogen rich medium, a different kind of emulsifier is produced. The exopolymer may contribute to hydrocarbons solubilization. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first exopolysaccharide with emulsifying properties produced by a Pseudomonas strain reported to the present. Also chemical composition is significantly different from previous reports. This strain has potential use in bioremediation and the purified polysaccharide may be used in food and cosmetic industry. Moreover, the production of the exopolymer may play a role on biofilm formation.     

Putting cells under pressure: a simple and efficient way to enhance the productivity of medium-chain-length polyhydroxyalkanoate in processes with Pseudomonas putida KT2440

The success of bioprocess implementation relies on the ability to achieve high volumetric productivities and requires working with high‐cell‐density cultivations. Elevated atmospheric pressure might constitute a promising tool for enhancing the oxygen transfer rate (OTR), the major growth‐limiting factor for such cultivations. However, elevated pressure and its effects on the cellular environment also represent a potential source of stress for bacteria and may have negative effects on product formation. In order to determine whether elevated pressure can be applied for enhancing productivity in the case of medium‐chain‐length polyhydroxyalkanoate (mcl‐PHA) production by Pseudomonas putida KT2440, the impact of a pressure of 7 bar on the cell physiology was assessed. It was established that cell growth was not inhibited by this pressure if dissolved oxygen tension (DOT) and dissolved carbon dioxide tension (DCT) were kept below ～30 and ～90 mg L^?1, respectively. Remarkably, a little increase of mcl‐PHA volumetric productivity was observed under elevated pressure. Furthermore, the effect of DCT, which can reach substantial levels during high‐cell‐density processes run under elevated pressure, was investigated on cell physiology. A negative effect on product formation could be dismissed since no significant reduction of mcl‐PHA content occurred up to a DCT of ～540 mg L^?1. However, specific growth rate exhibited a significant decrease, indicating that successful high‐cell‐density processes under elevated pressure would be restricted to chemostats with low dilution rates and fed‐batches with a small growth rate imposed during the final part. This study revealed that elevated pressure is an adequate and efficient way to enhance OTR and mcl‐PHA productivity. We estimate that the oxygen provided to the culture broth under elevated pressure would be sufficient to triple mcl‐PHA productivity in our chemostat system from 3.4 (at 1 bar) to 11 g L^?1 h^?1 (at 3.2 bar). Biotechnol. Bioeng. 2012; 109:451–461. © 2011 Wiley Periodicals, Inc.     

Production of Substituted Styrene Bioproducts from Lignin and Lignocellulose Using Engineered Pseudomonas putida KT2440

Ferulic acid is a renewable chemical found in lignocellulose from grasses such as wheat straw and sugarcane. Pseudomonas putida is able to liberate and metabolize ferulic acid from plant biomass. Deletion of the hydroxycinnamoyl‐CoA hydratase‐lyase gene (ech) produced a strain of P. putida unable to utilize ferulic and p‐coumaric acid, which is able to accumulate ferulic acid and p‐coumaric acid from wheat straw or sugar cane bagasse. Further engineering of this strain saw the replacement of ech with the phenolic acid decarboxylase padC, which converts p‐coumaric and ferulic acid into 4‐vinylphenol and the flavor agent 4‐vinylguaiacol, respectively. The engineered strain containing padC is able to generate 4‐vinylguaiacol and 4‐vinylphenol from media containing lignocellulose or Green Value Protobind lignin as feedstock, and does not require the addition of an exogenous inducer molecule. Biopolymerization of 4‐vinylguaiacol and 4‐vinylcatechol styrene products is also carried out, using Trametes versicolor laccase, to generate “biopolystyrene” materials on small scale.     

Production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) by Ralstonia eutropha in high cell density palm oil fermentations

Improved production costs will accelerate commercialization of polyhydroxyalkanoate (PHA) polymer and PHA-based products. Plant oils are considered favorable feedstocks, due to their high carbon content and relatively low price compared to sugars and other refined carbon feedstocks. Different PHA production strategies were compared using a recombinant strain of Ralstonia eutropha that produces high amounts of P(HB-co-HHx) when grown on plant oils. This R. eutropha strain was grown to high cell densities using batch, extended batch, and fed batch fermentation strategies, in which PHA accumulation was triggered by nitrogen limitation. While extended batch culture produced more biomass and PHA than batch culture, fed batch cultivation was shown to produce the highest levels of biomass and PHA. The highest titer achieved was over 139 g/L cell dry weight (CDW) of biomass with 74% of CDW as PHA containing 19 mol% HHx. Our data suggest that the fermentation process is scalable with a space time yield (STY) better than 1 g PHA/L/h. The achieved biomass concentration and PHA yield are among the highest reported for the fermentation of recombinant R. eutropha strains producing P(HB-co-HHx).     

Production of poly(3-hydroxybutyrate) and poly(3-hydroxybutyrate-co-4-hydroxybutyrate) by Ralstonia eutropha from soybean oil

High-yield production of polyhydroxyalkanoates (PHAs) by Ralstonia eutropha KCTC 2662 was investigated using soybean oil and γ-butyrolactone as carbon sources. In flask culture, it was shown that R. eutropha KCTC 2662 accumulated PHAs during the growth phase. The optimum carbon to nitrogen ratio (C/N ratio) giving the highest cell and PHA yield was 20 g-soybean oil/g-(NH(4))(2)SO(4). The 4-hydroxybutyrate (4HB) fraction in the copolymer was not strongly affected by the C/N ratio. In a 2.5-L fermentor, a homopolymer of poly(3-hydroxybutyrate) [P(3HB)] was produced from soybean oil as the sole carbon source by batch and fed-batch cultures of R. eutropha with dry cell weights of 15-32 g/L, PHA contents of 78-83 wt% and yields of 0.80-0.82 g-PHA/g-soybean oil used. By co-feeding soybean oil and γ-butyrolactone as carbon sources, a copolymer of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] could be produced with dry cell weights of 10-21 g/L, yields of 0.45-0.56 g-PHA/g-soybean oil used (0.39-0.50g-PHA/g-carbon sources used) and 4HB fractions of 6-10 mol%. Higher supplementation of γ-butyrolactone increased the 4HB fraction in the copolymer, but decreased cell and PHA yield.     

Metabolic engineering of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) composition in recombinant Salmonella enterica serovar typhimurium

A recombinant strain of Salmonella enterica serovar Typhimurium (mutant in propionate-activation activity) was metabolically engineered to control the composition of poly(3-hydroxybutyrate-co-3-hydroxy- valerate) (PHBV), a polyhydroxyalkanoate copolymer with commercially desirable properties. A gene (prpE) encoding propionyl-CoA synthetase was placed under the control of the IPTG-inducible taclacUV5 promoter (P(taclacUV5)) while the polyhydroxyalkanoate synthesis operon (phaBCA) from Acinetobacter sp. RA3849 was coexpressed under the control of the arabinose-inducible araBAD promoter (P(BAD)). S. enterica, harboring both constructs, was grown in medium containing a fixed substrate concentration and the composition of the copolymer was varied between 2 mol% and 25 mol% 3-hydroxyvalerate by controlling the IPTG level in the medium. This "dial-a-composition" system should find application in cases where the substrate concentration of a feedstream for PHBV bioplastic production is not adjustable.     

The Ssr protein (T1E_1405) from Pseudomonas putida DOT‐T1E enables oligonucleotide‐based recombineering in platform strain P. putida EM42

Some strains of the soil bacterium Pseudomonas putida have become in recent years platforms of choice for hosting biotransformations of industrial interest. Despite availability of many genetic tools for this microorganism, genomic editing of the cell factory P. putida EM42 (a derivative of reference strain KT2440) is still a time‐consuming endeavor. In this work we have investigated the in vivo activity of the Ssr protein encoded by the open reading frame T1E_1405 from Pseudomonas putida DOT‐T1E, a plausible functional homologue of the β protein of the Red recombination system of λ phage of Escherichia coli. A test based on the phenotypes of pyrF mutants of P. putida (the yeast's URA3 ortholog) was developed for quantifying the ability of Ssr to promote invasion of the genomic DNA replication fork by synthetic oligonucleotides. The efficiency of the process was measured by monitoring the inheritance of the changes entered into pyrF by oligonucleotides bearing mutated sequences. Ssr fostered short and long genomic deletions/insertions at considerable frequencies as well as single‐base swaps not affected by mismatch repair. These results not only demonstrate the feasibility of recombineering in P. putida, but they also enable a suite of multiplexed genomic manipulations in this biotechnologically important bacterium.     

重组嗜水气单胞菌Aeromonas hydrophila 4AK4中3-羟基丁酸3-羟基己酸共聚酯PHBHHx的发酵生产

3-羟基丁酸和3-羟基己酸共聚酯(PHBHHx)是一种性能优良的新型生物可降解材料,其机械和加工性能与3-羟基己酸(3HHx)在共聚物中的含量密切相关。在嗜水气单孢菌Aeromonas hydrophila 4AK4中引入了编码β-酮基硫解酶(β-ketothiolase)的phbA基因和编码乙酰乙酰辅酶A还原酶(Acetoacetyl-CoA reductase)的phbB基因,使重组菌增加了一条利用乙酰辅酶A合成3-羟基丁酸-CoA的代谢途径,这使得利用非相关性碳源调控PHBHHx的单体组成比例成为可能。利用葡萄糖酸钠和月桂酸作为碳源,对重组Aeromonas hydrophila 4AK4进行了摇瓶培养及5L发酵罐培养的研究。在摇瓶实验中,通过改变碳源中两种组分的比例,可以使A,hydrophila 4AK4合成的PHBHHx中的3HHx摩尔含量由原来的15％左右降低到3％～12％,成功地实现了对PHBHHx单体组成的调控;当以月桂酸为唯一碳源时,在5L发酵罐中,经过56h的培养,获得了51．5g／L的细胞干重(CDW),其中62％为PHBHHx,3HHx在PHBHHx中的摩尔含量为9．7％;当以1：1的葡萄糖酸钠和月桂酸为碳源时,48h的5L发酵罐培养获得了32．8g／L的CDW和52％的PHBHHx含量,其中3HHx在PHBHHx中的摩尔含量为6．7％。结果证明了该重组菌在大规模生产单体组成可控PHBHHx方面具有很大的应用潜力。