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.     

需钠弧菌(Vibrio natriegens)合成聚羟基丁酸的研究

研究结果表明,V.natriegens可以利用葡萄糖,果糖,以及糖蜜为碳源合成聚羟基丁酸[Poly(3HB)] ,当以糖蜜为碳源时,积累的Poly(3HB)达到细胞干重的28．4％,实验结果还表明,Poly(3HB)的积累滞后于细胞生长,在培养前加入过量的碳源,不仅没有Poly(3HB)积累,还抑制细胞的生长,测定了与Poly(3HB)合成相关的PHA聚合酶,β-酮硫解酶和乙酰乙酰CoA还原酶的活性。结果表明,伴随Poly(3HB)合成,PHA聚合酶活性从无到有,β－酮硫解酶活性提高了10倍以上。进一步通过利用脂肪酸合成代谢抑制物－浅蓝菌素（cerulenin),研究了脂肪酸从头合成途径与Poly(3HB)合成途径的关系。发现浅蓝菌素能够明显降低细胞Poly(3HB)的累积。根据以上结果,推测在V.natrigens中可能存在两条代谢途径参与Poly(3HB)的合成。     

Formation of blends of various poly(3-hydroxyalkanoic acids) by a recombinant strain of Pseudomonas oleovorans

Summary Recombinant strains of Pseudomonas oleovorans, which harbour the poly(3-hydroxybutyrate)-biosynthetic genes of Alcaligenes eutrophus, accumulated poly(hydroxyalkanoates), composed of 3-hydroxybutyrate(3HB), 3-hydroxyhexanoate (3HHx) and 3-hydroxyactanoate (3HO), up to 70% of the cell dry weight if the cells were cultivated with sodium octanoate as the carbon source. Physiological and chemical analysis revealed multiple evidence that this polymer is a blend of the homopolyester poly(3HB) and of the copolyester poly(3HHx-co-3HO) rather than a random or a block copolyester of 3HB, 3HHx and 3HO. The molar ratio between poly(3HHx-co-3HO) and poly(3HB) varied drastically during the process of fermentation. Whereas synthesis of poly(3HHx-co-3HO) started immediately after ammonium was exhausted in the medium, synthesis of poly(3HB) occurred only after a lag-phase. From freeze-dried cells poly(3HHx-co-3HO) was much more readily extracted with chloroform than was poly(3HB). The blend was fractionated into petrol-ether-insoluble poly(3HB) and petrol-ether-soluble poly(3HHx-co-3HO). The molecular weight values of these polyesters measured by gel permeation chromatography were 2.96 × 10⁶ and 0.35 × 10⁶ and were similar of those polymers accumulated by A. eutrophus or by wild-type P. oleovorans, respectively. Offprint requests to: A. Steinbüchel     

Hyperproduction of poly(4-hydroxybutyrate) from glucose by recombinant Escherichia coli

ABSTRACT: BACKGROUND: Poly(4-hydroxybutyrate) [poly(4HB)] is a strong thermoplastic biomaterial with remarkable mechanical properties, biocompatibility and biodegradability. However, it is generally synthesized when 4-hydroxybutyrate (4HB) structurally related substrates such as gamma-butyrolactone, 4-hydroxybutyrate or 1,4-butanediol (1,4-BD) are provided as precursor which are much more expensive than glucose. At present, high production cost is a big obstacle for large scale production of poly(4HB). RESULTS: Recombinant Escherichia coli strain was constructed to achieve hyperproduction of poly(4-hydroxybutyrate) [poly(4HB)] using glucose as a sole carbon source. An engineering pathway was established in E. coli containing genes encoding succinate degradation of Clostridium kluyveri and PHB synthase of Ralstonia eutropha. Native succinate semialdehyde dehydrogenase genes sad and gabD in E. coli were both inactivated to enhance the carbon flux to poly(4HB) biosynthesis. Four PHA binding proteins (PhaP or phasins) including PhaP1, PhaP2, PhaP3 and PhaP4 from R. eutropha were heterologously expressed in the recombinant E. coli, respectively, leading to different levels of improvement in poly(4HB) production. Among them PhaP1 exhibited the highest capability for enhanced polymer synthesis. The recombinant E. coli produced 5.5 g L-1 cell dry weight containing 35.4% poly(4HB) using glucose as a sole carbon source in a 48 h shake flask growth. In a 6-L fermentor study, 11.5 g L-1 cell dry weight containing 68.2% poly(4HB) was obtained after 52 h of cultivation. This was the highest poly(4HB) yield using glucose as a sole carbon source reported so far. Poly(4HB) was structurally confirmed by gas chromatographic (GC) as well as 1H and 13C NMR studies. CONCLUSIONS: Significant level of poly(4HB) biosynthesis from glucose can be achieved in sad and gabD genes deficient strain of E. coli JM109 harboring an engineering pathway encoding succinate degradation genes and PHB synthase gene, together with expression of four PHA binding proteins PhaP or phasins, respectively. Over 68% poly(4HB) was produced in a fed-batch fermentation process, demonstrating the feasibility for enhanced poly(4HB) production using the recombinant strain for future cost effective commercial development.     

Production of poly(3-hydroxybutyric acid-co-4-hydroxybutyric acid) and poly(4-hydroxybutyric acid) without subsequent degradation by Hydrogenophaga pseudoflava

A Hydrogenophaga pseudoflava strain was able to synthesize poly(3-hydroxybutyric acid-co-4-hydroxybutyric acid) [P(3HB-co-4HB)] having a high level of 4-hydroxybutyric acid monomer unit (4HB) from gamma-butyrolactone. In a two-step process in which the first step involved production of cells containing a minimum amount of poly(3-hydroxybutyric acid) [P(3HB)] and the second step involved polyester accumulation from the lactone, approximately 5 to 10 mol% of the 3-hydroxybutyric acid (3HB) derived from the first-step culture was unavoidably reincorporated into the polymer in the second cultivation step. Reincorporation of the 3HB units produced from degradation of the first-step residual P(3HB) was confirmed by high-resolution 13C nuclear magnetic resonance spectroscopy. In order to synthesize 3HB-free poly(4-hydroxybutyric acid) [P(4HB)] homopolymer, a three-stage cultivation technique was developed by adding a nitrogen addition step, which completely removed the residual P(3HB). The resulting polymer was free of 3HB. However, when the strain was grown on gamma-butyrolactone as the sole carbon source in a synthesis medium, a copolyester of P(3HB-co-4HB) containing 45 mol% 3HB was produced. One-step cultivation on gamma-butyrolactone required a rather long induction time (3 to 4 days). On the basis of the results of an enzymatic study performed with crude extracts, we suggest that the inability of cells to produce 3HB in the multistep culture was due to a low level of 4-hydroxybutyric acid (4HBA) dehydrogenase activity, which resulted in a low level of acetyl coenzyme A. Thus, 3HB formation from gamma-butyrolactone is driven by a high level of 4HBA dehydrogenase activity induced by long exposure to gamma-butyrolactone, as is the case for a one-step culture. In addition, intracellular degradation kinetics studies showed that P(3HB) in cells was completely degraded within 30 h of cultivation after being transferred to a carbon-free mineral medium containing additional ammonium sulfate, while P(3HB-co-4HB) containing 5 mol% 3HB and 95 mol% 4HB was totally inert in interactions with the intracellular depolymerases. Intracellular inertness could be a useful factor for efficient synthesis of the P(4HB) homopolymer and of 4HB-rich P(3HB-co-4HB) by the strain used in this study.     

Biosynthesis and n.m.r. studies of deuterated poly(3-hydroxybutyrate) produced by Alcaligenes eutrophus H16.

Alcaligenes eutrophus H16 was grown on mixtures of 1H- and 2H-acetate as carbon sources. The accumulation of deuterated poly(3-hydroxybutyrate) (P(3HB)) was observed. The deuterium distributions in the isolated P(3HB)s were determined from 1H and 2H-n.m.r. spectra and confirmed by 13C-n.m.r. spectra. Although one would expect to synthesize P([2,2,4,4,4-2H5]3HB) when the cells were grown on 2H-acetate as the sole carbon source, the methyl, methylene and methine groups of the P(3HB) contained both deuterium and proton. This observation indicates some substitution from 2H to 1H during the P(3HB) synthesis. The 2H content in the methyl groups was larger than that in the methylene groups, which suggests a kinetic isotope effect in the P(3HB) synthesizing process. The deuterium distributions in the two magnetically non-equivalent methylene protons were determined to be different, which indicates stereoselectivity at the C2 site.     

Fine structure and enzymatic degradation of poly[(R)-3-hydroxybutyrate] and stereocomplexed poly(lactide) nanofibers

Fiber morphology and crystalline structure of poly[(R)-3-hydroxybutyrate] (P(3HB)) and stereocomplexed poly(lactide) (PLA) nanofibers were investigated by using scanning and transmission electron microscopies and X-ray and electron diffractions. In the P(3HB) nanofibers spun from less than 1 wt% 1,1,1,3,3,3-hexafluoro-2-propanol (HFIP) solution, planar zigzag conformation (beta-form) as well as 2(1) helix conformation (alpha-form) structure was formed. Based on the electron diffraction measurement of single P(3HB) nanofiber, it was revealed that the molecular chains of P(3HB) align parallel to the fiber direction. From the enzymatic degradation test of P(3HB) nanofiber, it was shown that beta-form molecular chains are degraded more preferentially than alpha-form chains. Stereocomplexed PLA nanofibers were electrospun from 1 wt% poly(l-lactide)/poly(d-lactide) (PLLA/PDLA) solution in HFIP, which contains equal amounts of PLLA and PDLA. While as-spun stereocomplexed PLA nanofiber was amorphous, PLA nanofiber annealed at 100 degrees C contained only racemic crystal. It was supposed that the crystallization behavior of stereocomplexed PLA in the nanofiber is affected by the electrospinning process, which forcibly exerts the strain onto the polymer chains.     

Accumulation of a poly(hydroxyalkanoate) copolymer containing primarily 3-hydroxyvalerate from simple carbohydrate substrates by Rhodococcus sp. NCIMB 40126

A number of taxonomically-related bacteria have been identified which accumulate poly(hydroxyalkanoate) (PHA) copolymers containing primarily 3-hydroxyvalerate (3HV) monomer units from a range of unrelated single carbon sources. One of these, Rhodococcus sp. NCIMB 40126, was further investigated and shown to produce a copolymer containing 75 mol% 3HV and 25 mol% 3-hydroxybutyrate (3HB) from glucose as sole carbon source. Polyesters containing both 3HV and 3HB monomer units, together with 4-hydroxybutyrate (4HB), 5-hydroxyvalerate (5HV) or 3-hydroxyhexanoate (3HHx), were also produced by this organism from certain accumulation substrates. With valeric acid as substrate, almost pure (99 mol% 3HV) poly(3-hydroxyvalerate) was produced. N.m.r. analysis confirmed the composition of these polyesters. The thermal properties and molecular weight of the copolymer produced from glucose were comparable to those of PHB produced by Alcaligenes eutrophus.     

Biosynthesis and characterization of poly(d-lactate-co-glycolate-co-4-hydroxybutyrate)

Poly(d -lactate-co-glycolate-co-4-hydroxybutyrate) [poly(d -LA-co-GA-co-4HB)] and poly(d -lactate-co-glycolate-co-4-hydroxybutyrate-co-d -2-hydroxybutyrate) [poly(d -LA-co-GA-co-4HB-co-d -2HB)] are of interest for their potential applications as new biomedical polymers. Here we report their enhanced production by metabolically engineered Escherichia coli. To examine the polymer properties, poly(d -LA-co-GA-co-4HB) polymers having various monomer compositions (3.4–41.0mol% of 4HB) were produced by culturing the engineered E. coli strain expressing xylBC from Caulobacter crescentus, evolved phaC1 from Pseudomonas sp. MBEL 6-19 (phaC1437), and evolved pct from Clostridium propionicum (pct540) in a medium supplemented with sodium 4HB at various concentrations. To produce these polymers without 4HB feeding, the 4HB biosynthetic pathway was additionally constructed by expressing Clostridium kluyveri sucD and 4hbD. The engineered E. coli expressing xylBC, phaC1437, pct540, sucD, and 4hbD successfully produced poly(d -LA-co-GA-co-4HB-co-d -2HB) and poly(d -LA-co-GA-co-4HB) from glucose and xylose. Through modulating the expression levels of the heterologous genes and performing fed-batch cultures, the polymer content and titer could be increased to 65.76wt% and 6.19g/L, respectively, while the monomer fractions in the polymers could be altered as desired. The polymers produced, in particular, the 4HB-rich polymers showed viscous and sticky properties suggesting that they might be used as medical adhesives.     

以葡萄糖为唯一碳源合成聚-4-羟基丁酸的重组大肠杆菌的构建

为实现重组大肠杆菌以葡萄糖为唯一碳源合成均聚的P( 4HB) ,PCR扩增大肠杆菌编码谷氨酸:琥珀酰半缩醛转氨基酶基因(gabT) ,谷氨酸脱羧酶基因(gadA)以及富养罗尔斯通氏菌(Ralstoniaeutropha)H16的4_羟基丁酸脱氢酶基因(gadB) ,并组装到携带富养罗尔斯通氏菌(Ralstoniaeutropha)H16的PHA聚合酶基因(phaC)和克氏梭菌(Clostridiumkluyveri)中编码4_羟基丁酸:CoA转移酶基因(orfZ)的重组质粒pKESS5 3上,形成一个大的操纵元。携带重组质粒的大肠杆菌获得从三羧酸循环的中间物———α_酮戊二酸到P( 4HB)的代谢途径。结果表明,重组大肠杆菌可以以葡萄糖为唯一碳源合成均聚的P( 4HB) ,当向以葡萄糖为唯一碳源的无机培养基添加蛋白胨、酵母提取物、酪蛋白水解物时,P( 4HB)的含量可以高达菌体干重的30 %。     

Production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) from unrelated carbon sources by metabolically engineered Escherichia coli

A metabolically engineered Escherichia coli has been constructed for the production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] from unrelated carbon sources. Genes involved in succinate degradation in Clostridium kluyveri and P(3HB) accumulation pathway of Ralstonia eutropha were co-expressed for the synthesis of the above copolyester. E. coli native succinate semialdehyde dehydrogenase genes sad and gabD were both deleted for eliminating succinate formation from succinate semialdehyde, which functioned to enhance the carbon flux to 4HB biosynthesis. The metabolically engineered E. coli produced 9.4 g l^?1 cell dry weight containing 65.5% P(3HB-co-11.1 mol% 4HB) using glucose as carbon source in a 48 h shake flask growth. The presence of 1.5–2 g l^?1 α-ketoglutarate or 1.0 g l^?1 citrate enhanced the 4HB monomer content from 11.1% to more than 20%. In a 6 l fermentor study, a 23.5 g l^?1 cell dry weight containing 62.7% P(3HB-co-12.5 mol% 4HB) was obtained after 29 h of cultivation. To the best of our knowledge, this study reports the highest 4HB monomer content in P(3HB-co-4HB) produced from unrelated carbon sources.     

Biosynthesis of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) copolymer by Cupriavidus sp. USMAA1020 isolated from Lake Kulim, Malaysia

Cupriavidus sp. USMAA1020 was isolated from Malaysian environment and able to synthesize poly(3-hydroxybutyrate-co-4-hydroxybutyrate), [P(3HB-co-4HB)] when grown on gamma-butyrolactone as the sole carbon source. The polyester was purified from freeze-dried cells and analyzed by nuclear magnetic resonance (NMR) spectroscopy. 1H and 13C NMR results confirmed the presence of 3HB and 4HB monomers. In a one-step cultivation process, P(3HB-co-4HB) accumulation by Cupriavidus sp. USMAA1020 was affected by carbon to nitrogen ratio (C/N). A two-step cultivation process accumulated P(3HB-co-4HB) copolyester with a higher 4HB fraction (53 mol%) in nitrogen-free mineral medium containing gamma-butyrolactone. The biosynthesis of P(3HB-co-4HB) was also achieved by using 4-hydroxybutyric acid and alkanediol as 1,4-butanediol. The composition of copolyesters varied from 32 to 51 mol% 4HB, depending on the carbon sources supplied. The copolyester produced by Cupriavidus sp. USMAA1020 has a random sequence distribution of 3-hydroxybutyrate (3HB) and 4-hydroxybutyrate (4HB) units when analyzed by nuclear magnetic resonance (NMR) spectroscopy. When gamma-butyrolactone was used as the sole carbon source, the 4HB fraction in copolyester increased from 25 to 60 mol% as the concentration of gamma-butyrolactone in the culture medium increased from 2.5 g/L to 20.0 g/L.     

Production of poly(3-hydroxybutyrate) and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) by <Emphasis Type="Italic">Rhodopseudomonas palustris</Emphasis> SP5212

Summary Production of poly(3-hydroxybutyric acid) [P(3HB)] by Rhodopseudomonas palustris SP5212 isolated in this laboratory has been optimized under phototrophic microaerophilic conditions. Cells grown in malate medium accumulated 7.7% (w/w) P(3HB) of cellular dry weight at the early stationary phase of growth. The accumulated P(3HB) however, attained 15% (w/w) of cellular dry weight when acetate (1.0%, w/v) was used as the sole carbon source under nitrogen-limiting conditions. Synthesis and accumulation of polymer was favoured by sulphate-free conditions and at a phosphate concentration sub-optimal for growth. The polymer content of cells was increased drastically (34% of cellular dry weight) when the acetate containing medium was supplemented with n-alkanoic acids. Compositional analysis by H¹ NMR revealed that these accumulated polymers were composed of 3-hydroxybutyric acid and 3-hydroxyvaleric acid (3HV). The contents of 3HV in these copolymers ranged from 14 to 38 mol%.     

Production of copolymer poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-4-hydroxybutyrate) through a one-step cultivation process

A one-step cultivation process for the production of biodegradable polymer poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] by Cupriavidus sp. USMAA2-4 was carried out using various carbon sources. It was found that Cupriavidus sp. USMAA2-4 could produce approximately 44 wt.% copolymer of P(3HB-co-4HB) with 27 mol% 4HB composition when the combination of oleic acid and 1,4-butanediol are used as carbon sources in 60 h cultivation. The manipulation of carbon-to-nitrogen ratio (C/N) resulted in the increase of dry cell weight, PHA content as well as 4HB composition. A new strategy of introducing oleic acid and 1,4-butanediol together and separately at different concentration demonstrated different yield in PHA content ranging from 47 to 58 wt.%. The molecular weight obtained was 234 kDa (by adding 1,4-butanediol and oleic acid together) and 212 kDa (by adding 1,4-butanediol separately). The copolymer of P(3HB-co-4HB) produced by Cupriavidus sp. USMAA2-4 was detected statistically as a random copolymer when analysed by nuclear magnetic resonance (NMR) spectroscopy.     

Biosynthesis and mobilization of poly(3-hydroxybutyrate) [P(3HB)] by Spirulina platensis

Three strains of Spirulina platensis isolated from different locations showed capability of synthesizing poly(3-hydroxybutyrate) [P(3HB)] under nitrogen-starved conditions with a maximum accumulation of up to 10 wt.% of the cell dry weight (CDW) under mixotrophic culture conditions. Intracellular degradation (mobilization) of P(3HB) granules by S. platensis was initiated by the restoration of nitrogen source. This mobilization process was affected by both illumination and culture pH. The mobilization of P(3HB) was better under illumination (80% degradation) than in dark conditions (40% degradation) over a period of 4 days. Alkaline conditions (pH 10-11) were optimal for both biosynthesis and mobilization of P(3HB) at which 90% of the accumulated P(3HB) was mobilized. Transmission electron microscopy (TEM) revealed that the mobilization of P(3HB) involved changes in granule quantity and morphology. The P(3HB) granules became irregular in shape and the boundary region was less defined. In contrast to bacteria, in S. platensis the intracellular mobilization of P(3HB) seems to be faster than the biosynthesis process. This is because in cyanobacteria chlorosis delays the P(3HB) accumulation process.     

Degradation of poly(3-hydroxybutyrate) by soil streptomycetes

The ability of 64 soil streptomycetes to degrade poly(3-hydroxybutyrate) [P(3HB)] was evaluated on Pridham and Lyons mineral salts agar medium overlayered with the same medium containing 0.2% P(3HB). The streptomycete isolates were grown on this overlayered medium and the degradation was detected by the formation of clear zone surrounding the growth. Four potent degrader isolates identified as species of Streptomyces were selected. Degradation of P(3HB) by these isolates was studied for a period of 8 days. The rate of degradation increased with increase in concentration of P(3HB) in the medium while it decreased with the supplementation of readily utili- zable carbon sources like glucose, fructose and sucrose. All four isolates also degraded the copolymer of 3-hydroxybutyrate and 3-hydroxyvalerate [P(3HB–co–3HV)] in solid medium but to a lesser extent. However, the isolates were equally efficient in degrading P(3HB) in liquid medium.     

Economic considerations in the production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) by bacterial fermentation

The process for the production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB/V)] by bacterial fermentation and its recovery was analysed. The effects of various factors such as P(3HB/V) content, P(3HB/V) productivity, P(3HB/V) yield and 3-hydroxyvalerate (3HV) fraction in P(3HB/V) on the production cost of P(3HB/V) were examined. The increase in the 3HV yield on a carbon source did not significantly decrease the production cost when the 3HV fraction was 10 mol%, because the cost of the carbon substrate for 3HV was relatively small in terms of the total cost. However, at a 3HV fraction of 30 mol%, the 3HV yield on a carbon source had a significant effect on the total P(3HB/V) production cost. The production cost of P(3HB/V) increased linearly with the increase in the 3HV fraction in P(3HB/V). Received: 8 September 1999 / Received revision: 2 December 1999 / Accepted: 3 December 1999     

Engineering Escherichia coli for enhanced production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) in larger cellular space

Polyhydroxyalkanoates (PHA) are intracellularly accumulated as inclusion bodies. Due to the limitation of the cell size, PHA accumulation is also limited. To solve this problem, Escherichia coli was enlarged by over-expression of sulA gene to inhibit the cell division FtsZ ring assembly, leading to the formation of filamentary E. coli that have larger internal space for PHA accumulation compared with rod shape E. coli. As a result, more than 100% increases on poly(3-hydroxybutyrate) (PHB) contents and cell dry weights (CDW) were achieved compared with its control strain under same conditions. The enlarged cell strategy was applied to the production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) or P(3HB-co-4HB) by sad, gabD, essential genes ispH and folK knockout E. coli harboring two addictives and thus stable plasmids consisting of P(3HB-co-4HB) producing genes, including phaCAB operon, orfZ, 4hbD, sucD, essential genes ispH and folK as well as the sulA. The so constructed E. coli grew in glucose to form filamentary shapes with an improved P(3HB-co-4HB) accumulation around 10% more than its control strain without addition of 4HB precursor, reaching over 78% P(3HB-co-4HB) in CDW. Importantly, the shape changing E. coli was able to precipitate after 20 min stillstand. Finally, the filamentary recombinant E. coli was not only able to produce more P(3HB-co-4HB) from glucose but also allow convenient downstream separation from the fermentation broth.     

Extracellular poly(hydroxyalkanoate) depolymerases and their inhibitor from Pseudomonas lemoignei.

Enzymatic degradation processes of microbial copolyesters, poly(3-hydroxybutyrate-co-3-hydroxyvalerate): P(3HB-co-3HV) and poly(3-hydroxybutyrate-co-4-hydroxybutyrate): P(3HB-co-4HB), were studied by the weight loss (erosion) of copolyester films. These studies employed three extracellular depolymerases which degrade poly(3-hydroxybutyrate): P(3HB). Two enzymes were purified from the culture supernatant of Pseudomonas lemoignei and one from Alcaligenes faecalis T1. The rate of enzymatic degradation of microbial copolyester films with various compositions showed an almost similar tendency to three different P(3HB) depolymerases, and decreased in the following order: P(3HB-co-4HB) greater than P(3HB) greater than P(3HB-co-3HV). An inhibitory protein of P(3HB) depolymerases in the succinate culture medium of P. lemoignei was isolated and characterized. The molecular weight of P(3HB) depolymerase inhibitor was 35,000 as determined by polyacrylamide gel electrophoresis in the presence of sodium dodecyl sulphate. This inhibitor of a single polypeptide chain may reversibly bind the serine residues at the active site of P(3HB) depolymerase. This inhibitory protein was not induced in the culture medium when P. lemoignei was grown on P(3HB) as the sole carbon source.