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.     

Production of polyhydroxyalkanoates from intact triacylglycerols by genetically engineered Pseudomonas

Pseudomonas putida and P oleovorans have been extensively studied for their production of medium-chain-length (mcl)-polyhydroxyalkanoates (PHA). These bacteria are incapable of metabolizing triacylglycerols (TAGs). We have constructed recombinant P. putida and P. oleovorans that can utilize TAGs as substrates for growth and mcl-PHA synthesis. A recombinant plasmid, pCN51lip-1, carrying Pseudomonas lipase genes was used to electrotransform these organisms. The transformants expressed TAG-hydrolyzing activity as shown by a rhodamine B fluorescence plate assay. The genetically modified organisms grew in TAG-containing medium to a cell dry weight of 2-4 g/l. The recombinant P. putida produced mcl-PHA at a crude yield of 0.9-1.6 g/l with lard or coconut oil (Co) as substrate. While P. oleovorans transformant did not produce mcl-PHA, a mixed-culture fermentation approach with the wild-type and recombinant strains afforded polymer production from Co at a crude yield of 0.5 g/l. Compositional analysis by gas chromatography/mass spectrometry showed that beta-hydroxyoctanoate (31-45 mol %) and beta-hydroxydecanoate (28-35 mol %) were the dominant repeat units of the TAG-based PHA. The number-average and weight-average molecular masses of the PHAs as determined by gel permeation chromatography were 82-170 x 10(3) g/mol and 464-693 x 10(3) g/mol, respectively. The recombinant approach can greatly increase the number of organisms that can be used to produce PHA from fat and oil substrates.     

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.     

Biosynthesis of polyhydroxyalkanoates co-polymer in E. coli using genes from Pseudomonas and Bacillus

Expression of Pseudomonas aeruginosa genes PHA synthase1 (phaC1) and (R)-specific enoyl CoA hydratase1 (phaJ1) under a lacZ promoter was able to support production of a copolymer of Polyhydroxybutyrate (PHB) and medium chain length polyhydoxyalkanoates (mcl-PHA) in Escherichia coli. In order to improve the yield and quality of PHA, plasmid bearing the above genes was introduced into E. coli JC7623, harboring integrated beta-ketothiolase (phaA) and NADPH dependent-acetoacetyl CoA reductase (phaB) genes from a Bacillus sp. also driven by a lacZ promoter. The recombinant E. coli (JC7623ABC1J1) grown on various fatty acids along with glucose was found to produce 28-34% cellular dry weight of PHA. Gas chromatography and (1)H Nuclear Magnetic Resonance analysis of the polymer confirmed the ability of the strain to produce PHB-co-Hydroxy valerate (HV)-co-mcl-PHA copolymers. The ratio of short chain length (scl) to mcl-PHA varied from 78:22 to 18:82. Addition of acrylic acid, an inhibitor of beta-oxidation resulted in improved production (3-11% increase) of PHA copolymer. The combined use of enzymes from Bacillus sp. and Pseudomonas sp. for the production of scl-co-mcl PHA in E. coli is a novel approach and is being reported for the first time.     

Synthesis of short-/medium-chain-length poly(hydroxyalkanoate) blends by mixed culture fermentation of glycerol

Glycerol was used as a substrate in the bio-production of poly(hydroxyalkanoates) (PHAs) in an effort to establish an alternative outlet for glycerol and produce value-added products. Pseudomonas oleovorans NRRL B-14682 and Pseudomonas corrugata 388 grew and synthesized poly(3-hydroxybutyrate) (P3HB) and medium-chain-length PHA (mcl-PHA) consisting primarily of 3-hydroxydecanoic acid (C(10:0); 44 +/- 2 mol %) and 3-hydroxydodecenoic acid (C(12:1); 31 +/- 2 mol %), respectively, from glycerol at concentrations up to 5% (v/v). Cellular productivity maximized at 40% for P. oleovorans in 5% (v/v) glycerol and 20% for P. corrugata in 2% (v/v) glycerol after 72 h. Increasing the glycerol media concentration from 1% to 5% (v/v) caused a 61% and 72% reduction in the molar mass (M(n)) of the P3HB and mcl-PHA polymers, respectively. Proton-NMR analysis of the glycerol-derived P3HB revealed that the M(n) decrease was the result of esterification of glycerol onto the polymer in a chain terminating position. However, no evidence of glycerol-based chain termination was present in the mcl-PHA. The growth patterns of P. oleovorans and P. corrugata on glycerol permitted their use as mixed cultures to produce natural blends of P3HB and mcl-PHA. By incorporating a staggered inoculation pattern and varying the duration of the fermentations, P3HB/mcl-PHA ratios were achieved that varied from 34:66 to 96:4.     

Efficient production of medium-chain-length poly(3-hydroxyalkanoates) from octane by Pseudomonas oleovorans: economic considerations

Poly(3-hydroxyalkanoates) (PHA) have the potential to become a biodegradable alternative for conventional plastics. In order to produce PHA at competitive costs in comparison with commonly used plastics, efficient PHA production systems will have to be developed. Poly(3-hydroxybutyrate) fermentations are well developed and in actual use on an industrial scale; medium-chain-length PHA (mcl-PHA) production is less well described, although the vast majority of all PHA known today are mcl-PHA. This paper compares and describes mcl-PHA production systems with respect to the volumetric productivity, the cellular PHA content and the polymer yield on carbon substrates. Nitrogen was shown to be the most effective limitation to trigger PHA formation in P. oleovorans after different nutrient limitations had been compared. By using an economic model for the calculation of PHA production costs, we show that it should be possible to produce octane-based mcl-PHA on a large scale (more than 1000 tonnes/year) at costs below U.S. $ 10 kg⁻¹. Received: 4 April 1997 / Accepted: 20 May 1997     

Production of medium-chain-length polyhydroxyalkanoates by sequential feeding of xylose and octanoic acid in engineered Pseudomonas putida KT2440

ABSTRACT: BACKGROUND: Pseudomonas putida KT2440 is able to synthesize large amounts of medium-chain-length polyhydroxyalkanoates (mcl-PHAs). To reduce the substrate cost, which represents nearly 50% of the total PHA production cost, xylose, a hemicellulose derivate, was tested as the growth carbon source in an engineered P. putida KT2440 strain. RESULTS: The genes encoding xylose isomerase (XylA) and xylulokinase (XylB) from Escherichia coli W3110 were introduced into P. putida KT2440. The recombinant KT2440 exhibited a XylA activity of 1.47 U and a XylB activity of 0.97 U when grown on a defined medium supplemented with xylose. The cells reached a maximum specific growth rate of 0.24 h-1 and a final cell dry weight (CDW) of 2.5 g L-1 with a maximal yield of 0.5 g CDW g-1 xylose. Since no mcl-PHA was accumulated from xylose, mcl-PHA production can be controlled by the addition of fatty acids leading to tailor-made PHA compositions. Sequential feeding strategy was applied using xylose as the growth substrate and octanoic acid as the precursor for mcl-PHA production. In this way, up to 20% w w-1 of mcl-PHA was obtained. A yield of 0.37 g mcl-PHA per g octanoic acid was achieved under employed conditions. CONCLUSIONS: Sequential feeding of relatively cheap carbohydrates and expensive fatty acids is a practical way to achieve more cost-effective mcl-PHA production. This study is the first reported attempt to produce mcl-PHA by using xylose as the growth substrate. Further process optimizations to achieve higher cell density and higher productivity of mcl-PHA should be investigated. These scientific exercises will undoubtedly contribute to the economic feasibility of mcl-PHA production from renewable feedstock.     

Repressor titration: a novel system for selection and stable maintenance of recombinant plasmids.

The propagation of recombinant plasmids in bacterial hosts, particularly in Escherichia coli, is essential for the amplification and manipulation of cloned DNA and the production of recombinant proteins. The isolation of bacterial transformants and subsequent stable plasmid maintenance have traditionally been accomplished using plasmid-borne selectable marker genes. Here we describe a novel system that employs plasmid-mediated repressor titration to activate a chromosomal selectable marker, removing the requirement for a plasmid-borne marker gene. A modified E.coli host strain containing a conditionally essential chromosomal gene (kan) under the control of the lac operator/promoter, lac O/P, has been constructed. In the absence of an inducer (allolactose or IPTG) this strain, DH1 lackan , cannot grow on kanamycin-containing media due to the repression of kan expression by LacI protein binding to lac O/P. Transformation with a high copy-number plasmid containing the lac operator, lac O, effectively induces kan expression by titrating LacI from the operator. This strain thus allows the selection of plasmids without antibiotic resistance genes (they need only contain lac O and an origin of replication) which have clear advantages for use as gene therapy vectors. Regulation in the same way of an essential, endogenous bacterial gene will allow the production of recombinant therapeutics devoid of residual antibiotic contamination.     

Poly(ethylene glycol)-mediated molar mass control of short-chain- and medium-chain-length poly(hydroxyalkanoates) from Pseudomonas oleovorans

Three strains of Pseudomonas oleovorans, a well known poly(hydroxyalkanoate) (PHA) producer, were tested for the ability to control PHA molar mass and end group structure by addition of poly(ethylene glycol) (PEG) to the fermentation medium. Each strain of P. oleovorans - NRRL B-14682 (B-14682), NRRL B-14683 (B-14683), and NRRL B-778 (B-778) - synthesized a different type of PHA from oleic acid when cultured under identical growth conditions. Strain B-14682 produced poly(3-hydroxybutyrate) (PHB), while B-14683 synthesized a medium-chain-length PHA ( mcl-PHA) with a repeat unit composition ranging from C4 to C14 and some mono-unsaturation in the C14 alkyl side chains. Strain B-778 synthesized a mixture of PHB (95 mol%) and mcl-PHA (5 mol%). The addition of 0.5% (v/v) PEG (M(n) =200 g/mol, PEG-200) to the fermentation broth of strains B-14682 and B-778 resulted in chain termination through esterification at the carboxyl terminus of the PHB with PEG chain segments, thus reducing the molar mass by 54% and 23%, respectively. The molar mass of the mcl-PHA produced by strains B-14683 and B-778 also showed a 34% and 47% reduction in the presence of PEG-200, respectively, but no evidence of esterification was present. PEG-400 (M(n) =400 g/mol) had a reduced effect on PHA molar mass. In fact, the molar masses of the mcl-PHA derived from strain B-14683 and both the PHB and mcl-PHA from B-778 were unchanged by PEG-400. In contrast, the PHB produced by B-14682 showed a 35% reduction in molar mass in the presence of PEG-400.     

Very high-level production and export in Escherichia coli of a cellulose binding domain for use in a generic secretion-affinity fusion system

A novel expression vector pTugA, previously constructed in our laboratory, was modified to provide kanamycin resistance (pTugK) and used to direct the synthesis of polypeptides as fusions with the C- or N-terminus of a cellulose binding domain which serves as the affinity tag in a novel secretion-affinity fusion system. Fed-batch fermentation strategies were applied to production in recombinant E. coli TOPP5 of the cellulose binding domain (CBD) from the Cellulomonas fimi cellulase Cex. The pTugK expression vector, which codes for the Cex leader sequence that directs the recombinant protein to the periplasm of E. coli, was shown to remain stable at very high-cell densities. Recombinant cell densities in excess of 90 g (dry cell weight)/L were achieved using media and feed solutions optimized using a 2(n) factorial design. Optimization of inducer (isophenyl-thio-beta-D-galactopyranoside) concentration and the time of induction led to soluble, fully active CBD(Cex) production levels in excess of 8 g/L.     

Continuous bioconversion of n-octane to octanoic acid by recombinant Escherichia coli (alk(+)) growing in a two-liquid-phase Chemostat

Escherichia coli is able to grow on sugars in the presence of a bulk n-alkane phase. When E. coli is equipped with the alk genes from Pseudomonas oleovorans, the resulting recombinant strain converts n-alkanes into the corresponding alkanoic acids. To study the effects of growth rate and exposure to a bulk apolar phase on the physiology and the productivity of E. coli, we have grown this microorganism in two-liquid-phase continuous cultures containing 5% (v/v) n-octane.In contrast to batch cultures of wild-tape E. coli grown in the presence of n-octane, cells remained viable during the entire continuous culture, which lasted 200 h. Bioconversion of n-octane to n-octanoic acid by a recombinant E. coli (alk(+)) in a two-liquid-phase continuous culture was made possible by optimizing both the recombinant host strain and the conditions of culturing the organism. Continuous production in such two-phase systems has been maintained for the least 125 h without any changes in the product concentration in the fermentation medium. The volumetric productivity was determined as a function of growth rate and showed a maximum at a dilution rate D = 0.32 h(-1), reaching a continuous production rate of 0.5 g octanoate/L . h (4 tons/m(3) . year). (c) 1993 John Wiley & Sons, Inc.     

高产稳产聚羟基烷酸的重组大肠杆菌的构建

重组大肠杆菌Ｅｓｃｈｅｒｉｃｈｉａ ｃｏｌｉＨＭＳ１７４（ｐＴＺ１８ＵＰＨＢ） 含有携带聚羟基烷酸（ＰＨＡ） 合成基因（ ｐｈａＣＡＢ）＊＊ 的质粒ｐＴＺ１８ＵＰＨＢ,是很有潜力的ＰＨＡ 生产菌,但存在着质粒不稳定和不能合成３羟基丁酸（３ＨＢ） 与３羟基戊酸（３ＨＶ） 共聚物［Ｐ（３ＨＢｃｏ３ＨＶ）］ 的缺陷。将ＲＫ２ 质粒上的ｐａｒ ＤＥ 基因引入ｐＴＺ１８ＵＰＨＢ 构成质粒ｐＪＭＣ２ ,该质粒可以在宿主Ｅ．ＣｏｌｉＨＭＳ１７４ 中稳定遗传。将培养基中的磷酸盐浓度降至１８ ｍ ｍｏｌ／Ｌ,发现Ｅ．Ｃｏｌｉ ＨＭＳ１７４（ｐＪＭＣ２） 能够以丙酸为前体合成Ｐ（３ＨＢｃｏ３ＨＶ） ,其中３ＨＶ 在共聚物中的含量为５ ％ ～８ ％ 。在５Ｌ自动发酵罐中分批补料培养Ｅ．Ｃｏｌｉ ＨＭＳ１７４（ｐＪＭＣ２） ,培养基初始磷酸盐浓度为１５ ｍ ｍｏｌ／Ｌ,３０ ｈ 后每升培养液中干菌体可达４２－５ ｇ,Ｐ（３ＨＢｃｏ３ＨＶ） 占干重的７０ ％ ,其中３ＨＶ 在共聚物中的含量为４－９ ％ 。     

Effect of pH on the molecular weight of poly-3-hydroxybutyric acid produced by Alcaligenes sp.

Summary The molecular weight of a polymer is an important parameter characterizing the physical properties of the polymer. The effect of pH on the molecular weight of poly-3-hydroxybutyric acid (PHB) produced by Alcaligenes sp. K-912 were investigated. PHB having higher molecular weight was obtained when cultivated under high pH conditions compared to the results cultivated under low pH conditions. The polydispersity index was almost the same as 1.6. But the cell mass was decreased as the pH became higher. The molecular weight was mainly determined in the early cultivation period and molecular weight difference could be explained by calculating the number of polymer chains.     

Homologous recombination with linear DNA to insert antigenic protein in the flagellin: improvement of the Th1 immune response

Bacterial flagellin is a surface protein with numerous advantages for the presentation of exogenous peptides. However, the production of recombinant bacteria and the expression of fusion proteins is laborious and time consuming. Here, we present a simple way to produce modified bacteria. Partially deleted, non-functional, chromosomal flagellin gene (fliC ) was changed using homologous recombination by a functional linear fliC gene in which we introduced an exogenous oligonucleotide encoding for the peptide of interest. The modified fliC gene was produced by polymerase chain amplification. Linear amplicons were introduced into the non-motile E. coli by electroporation. The formation of functional flagellar filaments allowed the discrimination of motile transformants from non-motile, non-transformed cells. Thus antibiotic selection and gene expression inductors are not required since transformed bacteria can be easily isolated and used as a vector and adjuvant for immunization. To validate this hypothesis, we studied the immune response against the N-terminal peptide of Clostridium tyrobutyricum flagellin fragment. BALB/c mice were immunized either with the protein displayed as flagellin fusion protein on the surface of E. coli, with the recombinant protein in Freund's adjuvant (FA), or with the pcDNA3 vector bearing the DNA fragment encoding this protein. Immunization with the flagellin recombinant bacteria induced a strong Th1 response as measured by high level of IFN-gamma production and the lack of IL-4 production. The results indicate that the flagellar filament protein carrying a specific epitope can be a potent inducer of the Th1 cellular response.     

基因重组大肠杆菌表达HrpNEcc蛋白的发酵条件及诱导条件优化

对已构建好的表达HrpNEcc蛋白的工程菌BL21(DE3)/pET30a(+)hrpN Ecc的摇瓶发酵条件及乳糖诱导进行优化, 通过在7L发酵罐中放大发酵实验,以期提高蛋白产量并降低生产成本。在摇瓶中优化的发酵及诱导条件是：5% 的接种量,TB培养基,菌体培养至对数生长前期,添加3g/L外源诱导剂乳糖时,HrpNEcc蛋白产量可达417.60mg/L,比不添加乳糖时提高了36.73%,比用IPTG诱导时提高了16.85%。7L发酵罐中发酵,获得菌体湿重达到57.24g/L（WCW）,可溶性HrpNEcc蛋白产量占细胞总蛋白的50.2%,为3.29 g/L。     

Expression of recombinant human apolipoprotein A-I in Chinese hamster ovary cells and Escherichia coli.

Human recombinant apolipoprotein (apo) A-I was produced by Chinese hamster ovary (CHO) cells and Escherichia coli with expression vectors containing cDNAs encoding preproapoA-I or apoA-I, respectively. The apoA-I from CHO cells was purified from the culture medium by ammonium sulfate precipitation, phenyl-Sepharose chromatography, and affinity purification on anti-apoA-I immunoabsorber. Human apoA-I was produced in E. coli as a fusion protein with glutathione S-transferase. A four amino acid linker, which separated the two proteins, was specifically recognized and cut by Factor Xa. The purification was accomplished by chromatography of E. coli extracts on glutathione-Sepharose and digestion with Factor Xa. The highest production level was found to be 0.5 micrograms/ml of culture medium per 48 h for a clone of stable transformant of CHO cells, whereas E. coli could produce as much as 20 micrograms/ml of bacterial culture. These apoA-I forms were compared in terms of molecular weight, isoelectric point, and expression of several epitopes. Recombinant apoA-I obtained from CHO cells appears intact and its isoelectric point is compatible with that of the mature form and the proform of apoA-I, whereas a part of the apoA-I produced by E. coli does not contain the COOH-terminus. Also, two of six epitopes are expressed to a greater extent in apoA-I obtained from E. coli than in apoA-I obtained from human plasma.     

Synthesis of PHB by recombinant E. coli harboring an approximately 5 kb genomic DNA fragment from Streptomyces aureofaciens NRRL 2209

An approximately 5.0 kb Sau3A I genomic DNA fragment from Streptomyces aureofaciens NRRL 2209 was cloned in a plasmid vector and introduced into Escherichia coli. The recombinant E. coli accumulated polyhydroxyalkanoates (PHAs) as cytoplasmic inclusions. The accumulated PHA was identified as the isotactic homopolymer of PHB with a molecular weight of 2.85x10(5). Purified PHB granules were spherical with an average size of 1.1 microm and of stable configuration. DSC thermogram suggested high crystalline nature of the polymer. Maximum thermal degradation of the biopolymer occurred between 250 and 340 degrees C. Recombinant E. coli cells preferentially utilized glycerol as the carbon source and accumulated 25-28 times more PHB than the native S. aureofaciens.