WO1999014313A2 - Biological systems for manufacture of polyhydroxylalkanoate polymers containing 4-hydroxyacids - Google Patents

Biological systems for manufacture of polyhydroxylalkanoate polymers containing 4-hydroxyacids Download PDF

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WO1999014313A2
WO1999014313A2 PCT/US1998/019659 US9819659W WO9914313A2 WO 1999014313 A2 WO1999014313 A2 WO 1999014313A2 US 9819659 W US9819659 W US 9819659W WO 9914313 A2 WO9914313 A2 WO 9914313A2
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coli
coa transferase
coa
hydroxybutyrate
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WO1999014313A3 (en
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Gjalt W. Huisman
Frank A. Skraly
David P. Martin
Oliver P. Peoples
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Yield10 Bioscience Inc
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Metabolix Inc
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Priority to JP2000511853A priority patent/JP2001516574A/ja
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
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    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
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    • C12N15/09Recombinant DNA-technology
    • C12N15/63Introduction of foreign genetic material using vectors; Vectors; Use of hosts therefor; Regulation of expression
    • C12N15/79Vectors or expression systems specially adapted for eukaryotic hosts
    • C12N15/82Vectors or expression systems specially adapted for eukaryotic hosts for plant cells, e.g. plant artificial chromosomes (PACs)
    • C12N15/8241Phenotypically and genetically modified plants via recombinant DNA technology
    • C12N15/8242Phenotypically and genetically modified plants via recombinant DNA technology with non-agronomic quality (output) traits, e.g. for industrial processing; Value added, non-agronomic traits
    • C12N15/8243Phenotypically and genetically modified plants via recombinant DNA technology with non-agronomic quality (output) traits, e.g. for industrial processing; Value added, non-agronomic traits involving biosynthetic or metabolic pathways, i.e. metabolic engineering, e.g. nicotine, caffeine
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    • C12N9/10Transferases (2.)
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    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
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    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/62Carboxylic acid esters
    • C12P7/625Polyesters of hydroxy carboxylic acids

Definitions

  • poly- -hydroxybutyrate PHA
  • PHA poly- -hydroxybutyrate
  • n is 0 or an integer and R 1 , R 2 , R 3 , and R 4 are each selected from saturated and unsaturated hydrocarbon radicals; hal- and hydroxy-substituted radicals; hydroxy radicals; halogen radicals; nitrogen-substituted radicals; oxygen-substituted radicals; and hydrogen atoms,
  • PHA polymers have the ability to accumulate intracellular reserves of PHA polymers. Since polyhydroxyalkanoates are natural thermoplastic polyesters, the majority of their applications are as replacements for petrochemical polymers currently in use for packaging and coating applications. The extensive range of physical properties of the PHA family of polymers, in addition to the broadening of performance obtainable by compounding and blending as traditionally performed in the polymer industry, provides a corresponding broad range of potential end-use applications.
  • the PHAs can be produced in a wide variety of types depending on the hydroxyacid monomer composition
  • This wide range of polymer compositions reflects an equally wide range of polymer physical properties including: a range of melting temperatures from 40°C-180°C, glass transition temperatures from -35 to 5°C, degrees of crystallinity of 0% to 80% coupled with the ability to control the rate of crystallization and elongation to break of 5 to 500%.
  • Poly(3- hydroxybutyrate) for example, has characteristics similar to those of polypropylene while poly(3-hydroxyoctanoate) (a copolymer of (R)-3- hydroxyoctanoate and (R -3-hydroxyhexanoate) types behave more as elastomers and PHAs with longer side chains giving behavior closer to waxes.
  • the PHAs can also be plasticized and blended with other polymers or agents.
  • One particularly useful form is as a latex of PHA in water.
  • the monomer compositions also affect solubility in organic solvents allowing for a choice of a wide range of solvents.
  • Copolymers of (R)-3-hydroxybutyrate and other hydroxyacid comonomers have significantly different solubility characteristics from those of the PHB homopolymer.
  • PHAs have seen limited commercial availability with only the copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) being available in significant quantities.
  • This copolymer has been produced by fermentation of the bacterium Ralstonia eutropha (formerly Alcaligenes eutrophus). Fermentation processes for other PHAs have been developed (Williams and Peoples, 1996, CHEMTECH 26: 38-44). Plant crops are also being genetically engineered to produce these polymers, and offer a cost structure in line with the vegetable oils and direct price competitiveness with petroleum based polymers (Williams and Peoples 1996, CHEMTECH 26: 38-44).
  • polyesters have been manufactured using methods similar to that originally described for PHBV in which the microorganisms are fed a relatively expensive non-carbohydrate feedstock in order to force the incorporation of the monomer into the PHA polyester.
  • production of PHB4HB has been accomplished by feeding glucose and 4-hydroxybutyrate or substrate that is converted to 4-hydroxybutyrate to A. eutrophus (Kunioka, M. , Nakamura, Y. , and Doi, Y. 1988, Polym. Commun.
  • Substrates that are converted to 4-hydroxybutyrate are 1 ,4-butanediol, 1,6-hexanediol, 1,8- octanediol, 1,10-decanediol, 1,12-dodecanediol and 1,4-butyrolactone.
  • the PHB4HB copolymers can be produced with a range of monomer compositions which again provides a range of polymer properties. In particular as the amount of 4HB increases above 10 wt. %, the melting temperature (T m ) decreases below 130°C and the elongation to break increases above 400% (Saito, Y., Nakamura, S. , Hiramitsu, M. and Doi, Y. , 1996, Polym. Int. 39: 169).
  • PHA4HB was achieved in E. coli using the 4-hydroxybutyrate pathway from C. kluyve ⁇ (Hein, S., S ⁇ hling, B., Gottschalk, G. , and Steinbuchel, A.
  • a further object of the present invention is to provide techniques and procedures to stably engineer transgenic organisms that synthesize PHAs containing 4-hydroxybutyrate either as sole constituent or as co- monomer.
  • Transgenic E. coli strains are described in which the required phb genes have been integrated on the chromosome. Additional genes for the synthesis of the 4HB monomer are also integrated on the chromosome. The latter genes can be derived from a broad range of organisms which carry a 4-hydroxybutyryl-CoA transferase and be identified by screening for this activity in the engineered E. coli strains described here. In addition, an endogenous E. coli activity is disclosed that can be further improved for the purpose of 4HB-CoA transferase activity.
  • New pathways are also disclosed for the supply of intermediates of 4HB biosynthetic pathways such as ⁇ -ketoglutarate and ⁇ - aminobutyrate.
  • the diversity of these pathways is important for the successful production of 4HB containing PHAs from cheap carbon sources such as sugars and fatty acids.
  • Figure 1 A is the alignment of the C. kluyveri OrfZ sequence with the N-terminal sequence and internal sequences of 4-hydroxybutyryl CoA transferase (4HBCT) from C. aminobutyricum (SEQ LD Nos 1 and 2. Identical residues are indicated, similar residues are indicated by *.
  • Figures IB and 1C are the nucleotide sequence of the or Z gene from C. kluyeri.
  • Figure ID is the amino acid sequence of the orfL gene from C. isseyeri.
  • Figure 2 is a schematic of the endogenous synthesis of 4- hydroxybutyryl CoA from ⁇ -ketoglutarate through the GAB A shunt. 1. ⁇ - ketoglutarate aminotransferase; 2. glutamate decarboxylase; 3. GAB A transaminase; 4. Succinic semialdehyde reductase; 5. 4-hydroxybutyryl CoA transferase.
  • FIG 3 is a schematic of the endogenous synthesis of 4- hydroxybutyryl-CoA from GAB A precursors.
  • GABA is an intermediate in the degradation of amino acids such as arginine, glutamine and proline. Genes in arginine degradation are encoded by speA, adi, speB,pat zva ⁇ prr; genes in glutamine degradation are encoded by gltBD and gadB, genes in proline degradation are encoded by putA and gadB.
  • GABA is converted to 4-hydroxybutyryl-CoA by the gene products of gabT, 4hbD and hbcT.
  • Figure 4 is a schematic of the endogenous synthesis of 4- hydroxybutyryl CoA from succinate. 1. succinyl CoA-CoA transferase; 2. succinate semialdehyde dehydrogenase; 3. 4-hydroxybutyrate dehydrogenase; 4. 4-hydroxybutyryl CoA transferase.
  • Figure 5 is a schematic of the construction of plasmids for integration of the PHB synthase (phbC) gene from Z ramigera into the chromosome of E. coli and other Gram-negative bacteria.
  • phbC PHB synthase
  • Figures 6 and 6 A are a schematic of the construction of plasmids for integration of 3-ketoacyl-CoA thiolase (phbA) and acetoacetyl-CoA reductase (phbB) genes from Z. ramigera into the chromosome of E. coli and other Gram-negative bacteria.
  • phbA 3-ketoacyl-CoA thiolase
  • phbB acetoacetyl-CoA reductase
  • Figure 7 is a schematic of the metabolic and genetic representation of the engineered biosynthetic pathway for 4-hydroxybutyryl-CoA synthesis.
  • the gene products of gabT, 4hbD and hbcT are required for this pathway, gadAB and gdhA are helpful, whereas the gene products oiaspC, sad and gabD are preferably absent or inactive.
  • Figure 8 is a schematic of the construction of plasmids pMSX-TD and pMSXTpl-TD, which expresses enzymes to convert ⁇ -ketoglutarate to 4-hydroxybutyryl-CoA.
  • Figure 9 is a schematic of the construction of plasmids pMSX-ABT, pMSXTpl-ABT and pMSXTpl-BT, which expresses enzymes to convert ⁇ - ketoglutarate to 4-hydroxybutyryl-CoA.
  • RECTIFI Figure 10 is a schematic of the construction of plasmid pMSX- ABT and pMSX-ABT-TD which expresses enzymes to convert - ketoglutarate to 4-hydroxybutyryl-CoA.
  • Figure 11 is a schematic of the construction of plasmid pMSX- TIDD which expresses enzymes to convert succinate to 4-hydroxybutyryl- CoA
  • transgenic organisms that synthesize PHAs containing 4-hydroxybutyrate either as sole constituent or as co-monomer have been developed.
  • the transgenic organism is either a bacterium eg. Escherichia coli, K. pneumoniae, Ralstonia eutropha (formerly Alcaligenes eutrophus), Alcaligenes latus or other microorgamsms able to synthesize PHAs, or a higher plant or plant component, such as the seed of an oil crop (Brassica, sunflower, soybean, corn, safflower, flax, palm or coconut or starch accumulating plants (potato, tapioca, cassava).
  • an oil crop Brassica, sunflower, soybean, corn, safflower, flax, palm or coconut or starch accumulating plants (potato, tapioca, cassava).
  • a screening procedure for the identification of genes encoding enzymes capable of converting 4-hydroxybutyric acid to 4-hydroxybutyryl-CoA and methods for redirecting the flux of normal cellular metabolites such as e.g. succinic acid and/ or glutamic acid to 4-hydroxybutyric acid has been developed.
  • the gene encoding a 4-hydroxybutyryl CoA transferase gene from the Gram-positive, strict anaerobic bacterium Clostridium kluyveri has been identified and used to express this enzyme activity in a transgenic organism to convert 4-hydroxybutyric acid into 4- hydroxybutyryl-CoA resulting in the accumulation of poly(4- hydroxybutyrate) in E. coli.
  • a bacteria expressing a functional PHA synthase from a transgene is described, as well as methods for expressing these genes in transgenic plant crops. Screening systems for new 4-hydroxybutyryl CoA transferase encoding genes are also described.
  • Transgenic E. coli strains in which a PHA synthase encoding gene is integrated in the chromosome and expressed to levels supporting PHA synthesis have been developed. With these transgenic strains can be screened with genomic libraries from different biological sources for activities that convert alternative PHA precursors such as 4-hydroxybutyrate to corresponding substrates for PHA synthase.
  • a similar approach in metabolic engineering can accommodate production of 4HB containing PHAs in organisms such as A. eutrophus, A. latus and Comamonas which are currently capable of producing 4-hydroxybutyrate copolymers from cosubstrates and in transgenic microbial and plant crop systems expressing a PHA synthesis from a heterologous PHA synthase gene or genes.
  • the genes of interest can be expressed from extrachromosomal DNA molecules such as plasmids, which intrinsically results in a copy number effect and consequently high expression levels, or, more preferably, they can be expressed from the chromosome.
  • extrachromosomal DNA molecules such as plasmids
  • plasmids which intrinsically results in a copy number effect and consequently high expression levels
  • they can be expressed from the chromosome.
  • plasmid-based systems are unsatisfactory due to the extra burden of maintaining the plasmids and the problems of stable expression.
  • the minimal requirements for the synthesis of these PHAs in vivo includes a gene encoding 4-hydroxybutyrate CoA transferase or similar activity and 4- hydroxybutyrate.
  • the substrate 4-hydroxybutyrate can be administered to the PHA producing microorganism or be synthesized in vivo by engineered biosynthetic pathways from appropriate substrates. Amino acid sequence was determined for the purified 4-hydroxybutyrate CoA transferase (Scherf and Buckel, Appl. Environ. Microbiol. (1991) 57:2699-2701).
  • the purified protein was subjected to enzymatic digestion followed by amino acid sequence analysis of three of the resulting peptides.
  • the amino acid sequence of these peptides and the N-terminus of the intact protein showed a striking homology to the OrfZ gene product ( Figures 1 A, IB, 1C, and ID), whose identity and function was not known, thereby identifying orfZ as the gene encoding 4-hydroxybutyryl CoA transferase in C. khiyveri. This gene was renamed hbcT.
  • coli strain MBX777 contains the genes encoding ⁇ -ketothiolase, acetoacetyl CoA reductase and PHB synthase from Z ramigera. Upon introduction of a plasmid encoding hbcT and supplying 4-hydroxybutyrate in the growth medium, a PHB-4HB copolymer was formed.
  • 4-hydroxybutyrate is synthesized from endogenous intermediates instead of being supplied externally.
  • Two biochemical routes to the precursor 4HB-CoA can be established in a production organism for 4HB- containing PHAs. The first pathway proceeds from ⁇ -ketoglutarate, the second from succinate. Substrate for both pathways can also be provided through amino acid degradation.
  • Pathway to 4-hydroxybutyryl CoA from ot-ketoglutarate A pathway that enables the conversion of ⁇ -ketoglutarate to 4- hydroxybutyryl CoA is shown in Figure 2. Enzymes involved in this pathway are cc-ketoglutarate transaminase, glutamate dehydrogenase, glutamate decarboxylase, 4-hydroxybutyrate dehydrogenase and 4- hydroxybutyrate CoA transferase.
  • Genes encoding these activities can be acquired from multiple sources: gdhA gene encoding glutamate dehydrogenase: E. coli (Valle et al. Gene (1984) 27: 193-199 and Valle et al., Gene (1983) 23: 199-209), Klebsiella aerogenes (Mountain et al. , Mol. Gen. Genet. (1985) 199: 141- 145), Pyrococcus furiosus (DiRuggiero et al. , Appl. Environ. Microbiol. (1995) 61: 159-164; Eggen et al.
  • Glutamate dehydrogenase (Syntichaki et al. (1996) Gene 168: 87- 92), maize (Sakakibara et al. (1995), Plant Cell Physiol. 36: 789-797), human (Tzimagiogis et al. (1993), Hum. Genet. 91: 433-438), mouse (Tzimagiogis et al. (1991), Biochem. Biophys. Acta 1089: 250-253), Amuro et al. (1990), Biochem. Biophys. Acta 1049: 216-218).
  • ⁇ -ketoglutarate transaminase (Park et al. (1993), J. Biol. Chem.
  • the gab gene cluster is only expressed at low constitutive levels due to catabolite repression by glucose and ammonia. When a poor nitrogen source or succinate as carbon source are supplied the operon is derepressed.
  • both cAMP/CRP and NtrC regulate the promoter, in addition to a specific repressor encoded by gabC.
  • the promoter that regulates gabT is located upstream of gabD.
  • Succinate semialdehyde dehydrogenases are encoded by gabD and sad. These activities could be deleterious for the purpose of P4HB or PHB-4HB production although their expression is expected to be repressed by the presence of sufficient glucose and nitrogen sources.
  • Glutamate decarboxylase is a rare enzyme among the ⁇ nterobacteriacea. It is pyridoxal phosphate dependent and well expressed at low pH. Pathways to 4-hydroxybutyryl-CoA from arginine, putrescine, glutamine and proline via GABA
  • Bacteria such as Escherichia coli are capable of catabolizing at least four different amino acids (arginine, proline, glutamine, and glutamate) to produce GABA, which can be converted as described above to 4-hydroxy-butyryl-CoA. These catabolic pathways are depicted in Figure 3.
  • E. coli contains at least two activities, encoded by speA and adi, that can decarboxylate arginine to agmatine.
  • Putrescine and urea are formed from agmatine by the action of agmatine ureohydrolase, encoded by speB.
  • Putrescine donates an amino group to ⁇ -ketoglutarate to form 4- aminobutyraldehyde and glutamate in a reaction catalyzed by the product of the pat gene, putrescine aminotransf erase.
  • the 4-aminobutyraldehyde is oxidized to GABA by aminobutyraldehyde dehydrogenase, encoded by prr.
  • agmatine ureohydrolase putrescine aminotransf erase, and aminobutyraldehyde dehydrogenase is dually controlled by catabolite repression and nitrogen availability. Catabolite repression of agmatine ureohydrolase, but not that of putrescine aminotransf erase or aminobutyraldehyde dehydrogenase, can be relieved by cAMP.
  • Agmatine ureohydrolase synthesis is induced by arginine and agmatine.
  • Arginine decarboxylase synthesis is not sensitive to catabolite repression or to stimulation by nitrogen limitation or subject to substrate induction (Shaibe et al., J. Bacteriol.
  • Proline is degraded in E. coli by the product of the put A gene, which catalyzes successive oxidations of proline to pyrroline 5-carboxylate and then to glutamate.
  • the first step is FAD-dependent, and thus the PutA protein is membrane-associated.
  • This same protein also acts as a repressor of the put operon in the absence of proline.
  • the put operon is subject to catabolite repression (McFall and Newman, pp. 358-379, in Neidhardt, ed., Escherichia coli and Salmonella typhimurium: cellular and molecular biology, ASM Press, Washington, D.C. , 1996).
  • Glutamine is converted to glutamate in E. coli by glutamate synthase, the product of the gltB and gltD genes. Two molecules of glutamate are formed by the donation of an amino group by glutamine to ⁇ -ketoglutarate.
  • the activity of E. coli glutamate synthase is high when this organism is grown in ammonia-containing minimal medium and low when it is grown in the presence of glutamate or glutamate-generating nitrogen sources if nitrogen is limiting (Reitzer, pp. 391-407, in
  • oat Avena sativa
  • Brassicaceae Barbarea vulgaris, Nasturtium ojflcinale, Arabis drummondii, Aethionema grandiflora, Capsella bursa-pastoris, Arabidopsis arenosa, Sisymbrium altissimum, Thellungiella salsuginea, Polanisia dodecandra, Stanley a pinnata, Carica papaya, Brassica oleracea, Brassica nigra, Theobroma cacao) (Galloway et al. , Mol.
  • gltBD encoding glutamate synthase: Escherichia coli (Oliver et al. , Gene 60: 1, 1987), Aquifex aeolicus (Deckert et al. , Nature 392:353,
  • Haemophilus influenzae (Fleischmann et al., Science 269:496, 1995), Escherichia coli (Blattner et al. , Science 277: 1453, 1997), baker's yeast (Saccharomyces cerevisiae) (Science 265:2077, 1994), Vibrio alginolyticus (Nakamura et al. , Biochim. Biophys. Acta 1277:201, 1996), Pseudomonas aeruginosa (Savoiz et al. , Gene 86:107, 1990), Klebsiella pneumoniae (Chen and Maloy, J. Bacteriol.
  • arginine, proline, glutamine, or glutamate can be supplied exogenously to the poly(4-hydroxybutyrate)-producing organism, or it can be synthesized in the host from another carbon source, preferably an inexpensive one such as glucose. E. coli, for example, synthesizes all of these compounds from glucose, but generally only to an extent sufficient for growth.
  • E. coli that overproduce these compounds have been developed.
  • Tujimoto et al. (U.S. Patent 5,378,616) describe an E. coli mutant that accumulates glutamate.
  • Momose et al. (U.S. Patent 4,430,430) describe the overexpression of the argA gene in E. coli, which leads to arginine accumulation.
  • Proline-resistant mutants of E. coli that overexpress proline synthesis genes can accumulate proline (Wang et al., Chin. J. Biotechnol. 6:27, 1990). Tobacco plants which overexpress bacterial proline synthesis genes were also shown to accumulate proline (Sokhansandzh et al. , Genetika 33:906, 1997).
  • E. coli and other bacteria accumulate glutamate, GABA, and proline as a response to high medium osmolarity (McLaggan et al. , J. Biol. Chem. 269: 1911, 1994; Measures, J.C. , Nature 257:398, 1975; Schleyer et al. , Arch. Microbiol. 160:424, 1993; Botsford et al. , Appl. Environ. Microbiol. 60:2568, 1994).
  • glutamate-succinic semialdehyde transaminase genes can be isolated from gene libraries because of the ability of this gene to complement an E. coli gabT mutation for utilization of ⁇ -aminobutyric acid as nitrogen source.
  • mutations in glutamate dehydrogenase and glutamate decarboxylase genes in E. coli can be complemented.
  • Expression of alternative 4-hydroxybutyrate dehydrogenase genes will allow E. coli to utilize 4-hydroxybutyrate as a carbon source.
  • Enzyme homology searches using the BLASTP program and the GenBank database suggest the presence of 4-hydroxybutyrate dehydrogenase homologs in the E. coli genome. These proteins have been identified with the genetic index numbers: gi
  • Example 1 Minimal requirements for PHB-4HB synthesis
  • PHA poly-(R-3-hydroxybutyrate)
  • PHA poly-(R-3-hydroxybutyrate)
  • 4-Hydroxybutyryl-CoA can be prepared in situ from acetyl-CoA and 4- hydroxybutyrate via a transthioesterification reaction catalyzed by the enzyme 4-hydroxybutyryl-CoA transferase, isolated from Clostridium aminobutyricum. This enzyme will also catalyze the formation of (R)-3- hydroxybutyryl-CoA from the free acid and acetyl-CoA.
  • Example 2 Poly (4-hydroxybutyrate) (P4HB) synthesis in E. coli using a plasmid encoded pathway
  • the hbcT gene from C. kluyveri was expressed in E. coli using standard molecular biological techniques.
  • the gene is placed in an appropriate vector behind a strong promoter and under conditions that drive expression from this promoter. 4HBCT is produced.
  • Strains of E. coli were equipped with plasmid pFS30 which contains the genes encoding 4-hydroxybutyryl-CoA transferase from C. kluyveri and PHB synthase from R. eutropha. Theses genes are expected to convert 4-hydroxybutyric acid into 4-hydroxybutyryl-CoA which is subsequently polymerized to poly(4-hydroxybutyrate).
  • Strains were grown in 250 ml Erlenmeyer flasks containing 50 to 100 ml 10% LB liquid medium with 4-hydroxybutyrate, alone or in combination with glucose, as carbon source. Cultures were incubated at 30 to 33 ° C with shaking at 150 or 200 rpm. Cultures were harvested after 24 hours of incubation and analyzed for PHA.
  • E. coli MBX1177 (a spontaneous mutant of strain DH5 ⁇ selected for growth on minimal 4-HB medium) with pFS30 accumulates 67% of its cell dry weight as a P4HB homopolymer: host volume rpm 4HB glc T %LB %PHA F(4HB)
  • Example 3 Poly (4-hydroxybutyrate) (P4HB) synthesis in E. coli using a plasmid encoded PHA synthase.
  • Strains of E. coli were equipped with plasmid pFS16, which contains the gene encoding 4-hydroxybutyryl-CoA transferase from C. kluyveri. This gene is expected to convert 4-hydroxybutyric acid into 4- hydroxybutyryl-CoA which is subsequently polymerized by a chromosomally encoded PHB synthase into P4HB.
  • Strains were grown in 250 ml Erienmeyer flasks containing 50 to 100 ml 10% LB or 100% LB liquid medium with 4-hydroxybutyrate, alone or in combination with glucose, as carbon source. Cultures were incubated at 32 to 37 °C with shaking at 0 to 250 rpm.
  • Plasmid pMUXCscat contains the phbC gene from Z ramigera on a transposable element for integration of this gene on the chromosome of a recipient strain ( Figure 5). Strong translational sequences were obtained from pKPS4 which encodes PHA synthase encoding phaCl from . oleovorans in the pTrc vector (Pharmacia). In this construct, phaCl is preceded by a strong ribosome binding site: AGGAGGTTTTT(-ATG).
  • the phaCl gene including the upstream sequences, was cloned as a blunt ended EcoRI-Hindlll fragment in the Smal site of pUC 18 Sfi to give pMSXC 3 .
  • a blunt ended cat gene cassette was subsequently cloned in the blunt-ended Sse8387II site, resulting in pMSXC 3 cat.
  • all of the phaCl coding region except the 5' 27 base pairs were removed as a Pstl-BamHI fragment and replaced by the corresponding fragment from the phbC gene from Z ramigera.
  • the resulting plasmid, pMSXC 5 cat encodes a hybrid PHB synthase enzyme with the 9 amino terminal residues derived from the P. oleovorans PHA synthase and the remainder from Z ramigera.
  • the C 5 cat cassette was then excised as anAvrll fragment and cloned in the corresponding sites of pUTHg, thereby deleting the mercury resistance marker from this vector.
  • the resulting plasmid, pMUXC 5 cat contains a Cscat mini-transposon in which phbC is not preceded by a promoter sequence. Expression of the cassette upon integration is therefore dependent on transcriptional sequences that are provided by the DNA adjacent to the integration site.
  • pMSXTpiAB 5 kan2 was constructed from pMSXTpikan as follows
  • pMSXABscat was created by inserting a promoterless cat cassette in the Hindlll site of pMSXAB 5 .
  • the AB5 fragment from pMSXAB 5 cat was cloned as a EcoRI- Pstl fragment into the Smal site of pMSXTp ⁇ kan2 giving P MSXTp 1 AB 5 kan2.
  • Expression o ⁇ phbABS was improved by introduction of a strong promoter upstream of these genes ( Figures 6 and 6A).
  • This promoter was generated with sets of oligonucleotides that provide upstream activating sequences, a -35 promoter region, a -10 promoter region with transcriptional start site(s), and mRNA sequences with possible stabilizing functions.
  • Plasmid pMSXTpi AB 5 kan2 was digested with PstllXbal and a fragment containing the -10 region of the lac promoter was inserted as a fragment obtained after annealing oligonucleo-tides 3A (5 'GGCTCGTATAATGTGTGGAGGGAGAACCGCCGGGCTCGCCGTT) and
  • 3B (5' CTAGAACGGCGCGAGCCCGGCGGTTCTCCCTCCACA CATTATACGA GCCTGCA).
  • a fragment containing a consensus E. colipho box and -35 promoter region were inserted into the Pstl site as a fragment obtained after annealing the oligonucleotides: 2 A: (5' TCCCC TGTCATAAAGTTGTCACTGCA) and 2B (5' GTGACAACTTTATGACAGGGG ATGCA).
  • the messenger stabilizing sequence including the transcriptional start site from AB 5 was inserted into the Xbal-Ndel sites as a fragment obtained after annealing the oligonucleotides: 4A (5 ' : CTAGTGCCGG
  • the resulting plasmid is pMSXp ⁇ 2 AB 5 kan2.
  • the Avrll fragment, containing Tp ⁇ 2 AB 5 kan2 was cloned into pUTHg cut with Avrll and used for integration into the genome of MBX379 and MBX245.
  • DNA manipulations were performed on plasmid and chromosomal DNA purified with the Qiagen plasmid preparation or Qiagen chromosomal DNA preparation kits according to manufacturers recommendations. DNA was digested using restriction enzymes (New England Biolabs, Beverly, MA) according to manufacturers recommendations. DNA fragments were isolated from 0.7% agarose- Tris/acetate/EDTA gels using a Qiagen kit. Plasmid DNA was introduced into E. coli cells by transformation or electroporation (Sambrook et al.
  • phb genes from the pUT vectors was achieved by mating of the plasmid donor strain and the recipient (Herrero et al. J. Bacteriol. (1990) 172: 6557).
  • the recipient strains used were spontaneous naladixic acid or rifampicin resistant mutants of E. coli derived from either LS5218 or MBX23.
  • MBX23 is LJ14 rpoS: :Tnl0 in which the rpoS: :Tnl0 allele was introduced by PI transduction from strain 1106 (Eisenstark).
  • Recipients in which phb genes have been integrated into the chromosome were selected on naladixic acid or rifampicin plates supplemented with the antibiotic resistance specified by the mini-transposon, kanamycin or chloramphenicol. Oligonucleotides were purchased from Biosynthesis or Genesys. DNA sequences were determined by automated sequencing using a Perkin-Elmer ABI 373A sequencing machine. DNA was amplified using the synthase-chain- reaction in 50 microliter volume using PCR-mix from Gibco-BRL (Gaithersburg, Md) and an Ericomp DNA amplifying machine.
  • Accumulated PHA was determined by gas chromatographic (GC) analysis as follows. About 20 mg of lyophilized cell mass was subjected to simultaneous extraction and butanolysis at 110°C for 3 hours in 2 mL of a mixture containing (by volume) 90% 1-butanol and 10% concentrated hydrochloric acid, with 2 mg/mL benzoic acid added as an internal standard. The water-soluble components of the resulting mixture were removed by extraction with 3 mL water.
  • GC gas chromatographic
  • the organic phase (1 ⁇ L at a split ratio of 1:50 at an overall flow rate of 2 mL/min) was analyzed on an HP 5890 GC with FID detector (Hewlett-Packard Co, Palo Alto, CA) using an SPB-1 fused silica capillary GC column (30 m; 0.32 mm ID; 0.25 ⁇ m film; Supelco; Belief onte, Pa.) with the following temperature profile: 80 °C, 2 min; 10 C° per min to 250 °C; 250 °C, 2 min.
  • NTG l-Methyl-3-nitro-l-nitroso-guanidine
  • Results C 5 cat was introduced into the chromosome of MBX23 by conjugation using S17-1 ⁇ pir (pMUX cat) the donor strain.
  • the conjugation mixture was spread on LB/Nl/Cm plates and integrants were obtained of which 40% were sensitive to ampicillin, indicating that no plasmid was present in these strains.
  • Five integrants were transformed with pMSXAB 5 cat (Ap r ) and grown on LB/Ap/Cm/2% glucose to examine biosynthetic activity of PHB synthase.
  • MBX326 expressed the highest synthase activity and was used in further studies.
  • E. coli SI 7-1 ⁇ pir containing pMUXp i2 AB 5 kan was mated with MBX379.
  • Transgenic strains in which phbABJcan had integrated on the chromosome were selected on LB/Nl/Km plates.
  • PHB producers were identified on LB/glucose plates and MBX677
  • MBX379 : p 12 AB 5 kan
  • the PHB level in this strain grown in Luria-Bertani/2 % glucose medium was 58% whereas 38% PHB was accumulated in minimal medium supplemented with 2% glucose.
  • Example 6 Mutagenesis of transgenic E. coli strains for enhanced PHB production. Mutagenesis using NTG or EMS was used to improve PHB formation in MBX680. Strain MBX769 and MBX777 were selected after treatment of MBX680 with EMS and NTG respectively. These strains are able to grow on R2-medium supplied with 1 % glucose, 0.5% corn steep liquor and 1 mg/ml chloroamphenicol.
  • MBX769 was grown in 50 ml R-10 medium/ 0.5% CSL with 2 or 3 % glucose at 37 °C for 20 to 26 hours. PHB was accumulated to 71 % of the cell dry weight. Similarly, MBX769 was grown in 50 ml LB with or without 0.375 g/L KH 2 PO 4 , 0.875 K 2 HPO 4 and 0.25 (NH 4 ) 2 SO 4 and a total of 50 g/L glucose (five aliquots were added over the course of the incubation). After 63 hours of incubation, PHB had accumulated up to 96% of the cell dry weight. PHB levels in MBX777 strain grown in Luria-Bertani/2 % glucose medium was 67% whereas in minimal medium supplemented with 2% glucose 57% PHB was accumulated.
  • E. coli strains with a chromosomal phbC gene were obtained by PI transduction of the C5cat allele from MBX379 into LS5218, LS5218 / ⁇ ⁇ ; ⁇ /: :TnlO and LS5218 / ⁇ rfR + zcfll7: :TnlO.
  • the resulting strains are MBX816, MBX817 and MBX821, respectively.
  • Example 7 Poly (4-hydroxybutyrate) (P4HB) synthesis in E. coli using an endogenous 4-hydroxybutyryl-CoA transferase activity.
  • E. coli contains an endogenous gene encoding an enzyme with 4- hydroxybutyryl-CoA transferase activity.
  • Strains MBX821 and 1231 were grown in 250 ml Erienmeyer flasks containing 50 to 100 ml 10% LB liquid medium with 4-hydroxybutyrate, alone or in combination with glucose, as carbon source.
  • MBX1231 is a mutant of MBX821 obtained after treatment with l-methyl-3-mtro-l-nitrosoguanidine and selected on plates containing 500 ⁇ g/ml chloramphenicol. Cultures were incubated at 32 to 33 °C with shaking at 200 rpm. Cultures were harvested after 24 hours of incubation and analyzed for PHA. Table x shows that these strains accumulate 2.5 to 3.5% of the cell dry weight as a P4HB homopolymer.
  • P4HB formation in this strain is not dependent on a plasmid encoded PHB synthase nor a heterologously expressed 4- hydroxybutyryl-CoA transferase.
  • P4HB levels are improved to around 11 %.
  • Example 8 A screening method for air insensitive 4-hydroxybutyryl CoA transferase
  • the 4-hydroxybutyryl-CoA transferase from C. kluyveri appears to be inhibited by air, most likely by oxygen.
  • Oxygen insensitive mutants can be screened for by growing mutants of an E. coli strain that harbors the 4-hydroxybutyryl-CoA transferase encoding hbcT gene on a plasmid and a PHA synthase gene on the chromosome, for P4HB synthesis under high oxygenation conditions and searching for white colonies (indicative of PHA accumulation) where the majority of the population forms grey colonies.
  • Oxygen insensitive strains, MBX240 [pFS16], MBX379 [pFS16] and MBX830 [pFS16] were identified using this method.
  • mutants can be generated in vivo by treating the original strain with chemical mutagens such as N-methyl-N'-nitro-N- nitrosoguanidine or ethylmethanesulfonate or with ultraviolet radiation.
  • chemical mutagens such as N-methyl-N'-nitro-N- nitrosoguanidine or ethylmethanesulfonate or with ultraviolet radiation.
  • an hbcT containing plasmid can be mutagenized in vitro with hydroxylamine.
  • Mutants expressing a functional 4-hydroxybutyryl- CoA transferase are then screened for on solid media or highly oxygenated liquid media for P4HB formation from 4-hydroxybutyrate.
  • Example 9 A screening method for additional E. coli genes encoding 4- hydroxybutyryl CoA biosynthetic enzymes
  • Expression of the enzymatic activity that converts 4HB to 4HB- CoA in MBX821 or 1231 may be elevated by mutagenesis. Appearance of P4HB in MBX821 and 1231 grown on solid media took approximately 150 hours. Mutants with improved P4HB accumulation characteristics can be screened for after random mutagenesis of these strains with chemical mutagens such as N-methyl-N'-mtro-N-nitrosoguanidine or ethylmethanesulfonate or with ultraviolet radiation. Desired mutants form white colonies within 2 to 5 days of incubation in the presence of 4- hydroxybutyrate.
  • Example 10 A screening method for other genes encoding 4- hydroxybutyryl CoA biosynthetic enzymes Because applications involving plant systems require DNA with a high GC content, alternative 4-hydroxybutyryl CoA biosynthetic genes need to be identified and isolated. The low GC content of the hbcT gene would makes it a useful probe for identification and isolation of homologous genes from other AT-rich DNA containing microorgamsms. HbcT genes with a high GC content however will not be identified by this method. E. coli strains that have a chromosomally integrated phbC gene encoding PHA synthase can be used to screen for such genes.
  • MBX379 for instance, this strain is able to produce a P4HB polymer on agar plates containing 4-hydroxybutyrate in addition to the common nutrients.
  • the formation of P4HB gives the colony an easily distinguishable white phenotype.
  • gene libraries of PHB-co-4HB producing organisms such as R. eutropha, A. latus, P. acidovorans, C. testosteroni and others are introduced into MBX379 or similar strains and directly plated on 4HB containing growth medium. White colonies are selected and the composition of the accumulated PHA is determined.
  • Gene libraries are readily constructed from organisms of choice by isolating genomic DNA and cloning a representative collection of DNA fragments in plasmid vectors.
  • Libraries should have 5,000 to 100,000 individual colonies. Libraries are either made as a broad host range library in vectors such as pLAFR3 or as E. coli libraries in vectors such as pUC19, pBR322. Depending on the type of library and the method of introducing the library in the host of choice, the genomic DNA fragments are either large (17-30 kb) or relatively small (2-6 kb). Libraries are introduced into the screening strains by electroporation, transformation or conjugation, dependent on the host and the vector used. In addition to alternative 4-hydroxybutyryl CoA transferases, acyl CoA synthetases able to utilize 4-hydroxybutyrate as a substrate will be isolated by this method.
  • genes encoding enzymes with such general activities are fadD, involved in uptake of long-side chain fatty acids, atoDA, involved in uptake of acetoacetate and short side chain fatty acids, catE, involved in degradation of aromatics, aceAB, encoding succinyl CoA synthetase, acsA and acsB encoding acetyl CoA synthetases and homologs of such genes.
  • the substrate specificity of these enzymes may be expanded to include 4-hydroxybutyrate by introducing plasmids with randomly mutagenized acyl CoA synthetase or transferase genes.
  • the ygfH gene from E.
  • Example 11 Endogenous synthesis of 4HB-CoA from a-ketoglutarate ⁇ -Ketoglutarate is a cellular metabolite that can be converted to 4HB as shown in Figure 7.
  • the pathway consists of a cyclic reaction catalyzed by the gabT, gadA/gadB and gdhA gene products.
  • succinic acid semialdehyde from this cycle is favored once the product is further converted to 4HB-CoA by 4-HB dehydrogenase and 4HB-CoA transferase, and polymerized into a PHA by PHA synthase.
  • 4hbD was obtained from pCK3 by PCR using the primers: 4HBD-N: 5 ' CTCTG AATTC AAGGAGGAAAAAATATG AAGTTAT TAAAATTGGC (EcoRl)
  • 4HBD-C 5 'TTTCTCTGAGCTCGGGATATTTAATGATTGTAGG
  • the TD or TP r TD fragment was excised as a Avrll fragment and ligated into Avrll digested pUTkan (pMUX-TD and pMUX-TPj-TD).
  • This plasmid allows random insertion of the TD/TPl - TD construct in the chromosome of E. coli.
  • Expression of integrated TD is driven by an endogenous promoter whereas expression of integrated TPj-TD is driven by P, .
  • Recombinants in which the construct had integrated were selected for their ability to grow on 4-hydroxybutyrate as sole carbon source. No antibiotic resistance marker was required to select the desired insertions.
  • genes encoding enzymes that facilitate conversion of succinic semialdehyde to 4-hydroxybutyryl CoA can be isolated routinely by complementation. After introduction of 4hbD homologs such genes confer on wild-type E. coli strains the ability to use 4HB as sole carbon source.
  • gdhA- gadA- gabT An operon consisting of gdhA- gadA- gabT was created in plasmid pUC18Sfi and inserted in the E. coli chromosome using the pUTkan vector. Recipients of the construct were isolated on ⁇ 2/glycerol/_ ⁇ - hydroxybutyrate /Nl plates. Because the recipient strain is unable to use ⁇ -hydroxybutyrate as nitrogen source (due to a gabT mutation), only those strains that express the operon grow on this medium.
  • the gdhA gene was obtained from the E. coli chromosome using PCR and the following primers: GH-Up: 5' AACGAATTCAATTCAGGAGGTTTTTATGGATCAGAC ATATTCTCTGGAGTC (EcoRT)
  • GH-Dn 5' TTGGGAGCTCTACAGTAAGAAATGCCGTTGG (Sad).
  • the gadB gene was obtained from the E. coli chromosome using PCR and the following primers: GB-Up: 5' TAAGAGCTCAATTCAGGAGGTTTTTATGGATAAGAA GCAAGTAACGGATTTAAGG (Sad)
  • GB-Dn 5' TTCCCGGGTTATCAGGTATGCTTGAAGCTGTTCTGT TGGGC (Xmal).
  • the gabT gene was obtained from the E. coli chromosome using PCR and the following primers: GT-Up: 5' TCCGGATCCAATTCAGGAGGTTTTTATGAACAGCAA
  • TAAAGAGTTAATGCAG (BamHT) GT-Dn: 5' GATTCTAGATAGGAGCGGCGCTACTGCTTCGCC
  • DNA sequence information used to design the above primers was from GenBank, accession numbers: K02499 (gdhA), M84025 and X71917 (gadB), M88334 (gabT).
  • the operon was excised as an EcoRI-Sall fragment and cloned in pMSXTP, (pMSX-TP r ABT). Either the ABT or TP r ABT insert was moved to pUTkan to allow insertion of the gdhA- gadA- gabT operon in the chromosome of a gabT mutant of E. coli MBX245. Successful insertions were selected on E2/glycerol/ ⁇ -hydroxybutyrate /Nl plates.
  • gabT expression allows the use of ⁇ -hydroxybutyrate as nitrogen source, genes that express this function can be easily selected for on minimal medium plates in which ⁇ -hydroxybutyrate serves as the only nitrogen source. Expression of gabT at the end of the operon necessitates the transcription of the upstream genes for which no direct selection is available.
  • Glutamate dehydrogenase functions in this pathway as a source to provide glutamate in catalytic amounts. If sufficient glutamate is present, additional GdhA activity may not be required and incorporation of this gene in the described constructs is therefore optional.
  • Example 12 Endogenous synthesis of 4HBCoA from GABA precursors
  • the common metabolite GABA is derived from glutamate and is normally metabolized via succinic semialdehyde to succinate in central metabolism. It may be desirable to improve the pathways to GABA to achieve high levels of the intermediates for P4HB formation. Besides the direct conversion of ⁇ -ketoglutarate to glutamate by glutamate dehydrogenase, this conversion is also part of many transamination reactions for instance with substrates such as glutamine and other amino acids, or putrescine.
  • HbcT is not required for E. coli to grow on 4-hydroxybutyrate when catl, 4hbD and sucD are introduced (S ⁇ hling and Gottschalk, 1996, J. Bacteriol. 178, 871-880) possibly because the reverse action of SucD, 4HBD and Catl converts 4HB to succinate, a central metabolite in E. coli.
  • these genes together allow the conversion of succinate to 4-HB.
  • the pathway as depicted in Figure 4 can then be assembled from the catl, sucD, 4hbD and hbcT genes of C. kluyveri. Alternatively, these genes can be isolated from other Clostridium species such as C. aminobutyricum.
  • E. coli does have a succinyl-CoA:CoA transferase itself (sucCD; Mat- Jan et al. Mol. Gen. Genet. (1989) 215: 276-280), it is desirable to introduce this gene from another source because this activity is not prominent in E. coli (Amarasingham and Davis, J. Biol. Chem. (1965) 240: 3664-3668). Alternatively, expression of the E. coli gene can be optimized for the current application.
  • a BamHI-Pstl fragment from pCK3 containing orfY, catl, sucD and the 5' end of 4hbD was ligated in the corresponding sites of pMSXcat (pMSX-YlD).
  • the 4hbD gene was completed by inserting the Pstl-Sad fragment of pMSX-D in Pstl-Sphl digested pMSX-YlD (pMSX-YIDD). To achieve this, both fragments in this ligation were T4 polymerase treated after the Sphl and Sad digestions to create blunt ends before an additional Pstl digestion was started.
  • OrfY in pMSX-YIDD was replaced with hbcT by digesting pMSX-YIDD with BamHI and Pad, followed by blunt ending the fragment with Klenow/T4 polymerase and dephosphorylation, and then ligation of the SspI/EcoRI, Klenow treated hbcT fragment into this vector (pMSX-TIDD).
  • a fragment providing the regulatory sequences, terminator and promoter was inserted as a blunt ended fragment in the Smal site of pMSX-TIDD.
  • An integration plasmid for this operon was constructed by cloning the insert of pMSX-TIDD as an Sfil fragment into pUTkan.
  • Example 14 Improved endogenous synthesis of 4HBCoA
  • the aspC gene maps to minute 21.1 and is therefore linked to the TnlO (Tc) marker in CAG 12094 (zcc-282 at 22.25 minutes) or CAG18478 (zbj-1230 at 20.00 minutes) and to the TnlOKm marker in CAG12130 (zcb-3111 at minute 21.00).
  • Tc TnlO
  • CAG 12094 zcc-282 at 22.25 minutes
  • CAG18478 zbj-1230 at 20.00 minutes
  • TnlOKm marker in CAG12130
  • No mutations in the gabD gene are known and deletion of this activity can be achieved by cloning the gene by PCR, insertion of a genetic marker such as antibiotic resistance, integration using recBC strains or vectors constructed for this purpose such as pMAK705 and finally, bacteriophage PI transduction to transfer the gene to the desired host.
  • Example 15 Expression of A PHA synthase and 4-hydroxybutyryl- CoA transferase in Oilseed Crops.
  • Methods for the identification of genes encoding enzymes capable of forming 4-hydroxybutyryl-CoA from 4-hydroxybutyric acid (i.e. , having 4-hydroxybutyryl-CoA transferase activity) which can be expressed in a transgenic plant comprising a PHA synthase transgene were developed by standard procedures. In certain cases, it may also be useful to express other PHA biosynthetic genes such as a ⁇ -ketothiolase and/or acetoacetyl-CoA reductase in the plant crop of interest.
  • a gene or genes in the case of a PHA synthase with more than one subunit, encoding a PHA synthase from a microorganism into plant cells and obtain the appropriate level of production of the PHA synthase enzyme.
  • additional PHA biosynthetic genes eg. an acetoacetyl-CoA reductase gene, a 4- hydroxybutyryl-CoA transferase gene or other genes encoding enzymes required to synthesize the substrates for the PHA synthase enzymes.
  • More recent technology enables the direct insertion of foreign genes directly into the plastid chromosome by recombination (Svab et. al. , 1990, Proc. Natl;. Acad. Sci. USA. 87: 8526-8530; McBride et. al., 1994, Proc. Natl. Acad Sci. USA. 91: 7301-7305).
  • the prokaryotic nature of the plastid RNA and protein synthesis machinery also allows for the expression of microbial operons such as for example the phbCA operon of A. eutrophus. This technology allows for the direct incorporation of a series of genes encoding a multi-enzyme pathway into the plastid genome.

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Families Citing this family (129)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7455999B2 (en) * 1998-01-22 2008-11-25 Metabolix, Inc. Transgenic systems for the manufacture of poly (3-hydroxy-butyrate-co-3-hydroxyhexanoate)
DK1163019T3 (da) 1999-03-25 2008-03-03 Metabolix Inc Medicinske indretninger og anvendelser af polyhydroxyalkanoatpolymere
US7867250B2 (en) 2001-12-19 2011-01-11 Nmt Medical, Inc. Septal occluder and associated methods
US7318833B2 (en) 2001-12-19 2008-01-15 Nmt Medical, Inc. PFO closure device with flexible thrombogenic joint and improved dislodgement resistance
CA2471871A1 (en) * 2002-01-14 2003-07-24 Nmt Medical, Inc. Patent foramen ovale (pfo) closure method and device
US9241695B2 (en) 2002-03-25 2016-01-26 W.L. Gore & Associates, Inc. Patent foramen ovale (PFO) closure clips
US7431729B2 (en) 2002-06-05 2008-10-07 Nmt Medical, Inc. Patent foramen ovale (PFO) closure device with radial and circumferential support
AUPS318202A0 (en) * 2002-06-26 2002-07-18 Cochlear Limited Parametric fitting of a cochlear implant
US7766820B2 (en) 2002-10-25 2010-08-03 Nmt Medical, Inc. Expandable sheath tubing
US20040093017A1 (en) * 2002-11-06 2004-05-13 Nmt Medical, Inc. Medical devices utilizing modified shape memory alloy
US9017373B2 (en) 2002-12-09 2015-04-28 W.L. Gore & Associates, Inc. Septal closure devices
US9861346B2 (en) 2003-07-14 2018-01-09 W. L. Gore & Associates, Inc. Patent foramen ovale (PFO) closure device with linearly elongating petals
ES2428967T3 (es) 2003-07-14 2013-11-12 W.L. Gore & Associates, Inc. Dispositivo tubular de cierre de foramen oval permeable (FOP) con sistema de retención
US8480706B2 (en) 2003-07-14 2013-07-09 W.L. Gore & Associates, Inc. Tubular patent foramen ovale (PFO) closure device with catch system
EP1660167B1 (en) 2003-08-19 2008-11-12 NMT Medical, Inc. Expandable sheath tubing
US7745197B1 (en) * 2003-10-15 2010-06-29 Newlight Technologies, Llc Process for the utilization of ruminant animal methane emissions
US8735113B2 (en) 2003-10-15 2014-05-27 Newlight Technologies, Llc Methods and systems for production of polyhydroxyalkanoate
US7579176B2 (en) * 2003-10-15 2009-08-25 Newlight Technologies, Llc Method for the production of polyhydroxyalkanoic acid
US20050273119A1 (en) 2003-12-09 2005-12-08 Nmt Medical, Inc. Double spiral patent foramen ovale closure clamp
US7871419B2 (en) 2004-03-03 2011-01-18 Nmt Medical, Inc. Delivery/recovery system for septal occluder
US20050267524A1 (en) 2004-04-09 2005-12-01 Nmt Medical, Inc. Split ends closure device
US8361110B2 (en) 2004-04-26 2013-01-29 W.L. Gore & Associates, Inc. Heart-shaped PFO closure device
US7842053B2 (en) 2004-05-06 2010-11-30 Nmt Medical, Inc. Double coil occluder
US8308760B2 (en) 2004-05-06 2012-11-13 W.L. Gore & Associates, Inc. Delivery systems and methods for PFO closure device with two anchors
JP2007535997A (ja) 2004-05-07 2007-12-13 エヌエムティー メディカル, インコーポレイティッド 管状中隔オクルーダーの捕捉機構
JP4720114B2 (ja) * 2004-05-20 2011-07-13 三菱化学株式会社 オキザロ酢酸またはオキザロ酢酸誘導体の製造方法
ATE473021T1 (de) 2004-08-03 2010-07-15 Tepha Inc Nichtkräuselnde polyhydroxyalkanoatnähte
US8764848B2 (en) 2004-09-24 2014-07-01 W.L. Gore & Associates, Inc. Occluder device double securement system for delivery/recovery of such occluder device
US8277480B2 (en) 2005-03-18 2012-10-02 W.L. Gore & Associates, Inc. Catch member for PFO occluder
KR100979694B1 (ko) 2005-05-24 2010-09-02 한국과학기술원 폴리락테이트 또는 그 공중합체 생성능을 가지는 세포 또는식물 및 이를 이용한 폴리락테이트 또는 그 공중합체의제조방법
DK2781593T3 (da) * 2005-08-22 2019-10-21 Newlight Tech Inc Fremgangsmåde til behandling af methanemissioner
JP2009512521A (ja) * 2005-10-24 2009-03-26 エヌエムティー メディカル, インコーポレイティッド 放射線不透過性生体吸収性オクルダ
WO2007073566A1 (en) * 2005-12-22 2007-06-28 Nmt Medical, Inc. Catch members for occluder devices
US8979921B2 (en) * 2006-02-07 2015-03-17 Tepha, Inc. Polymeric, degradable drug-eluting stents and coatings
WO2007092417A1 (en) * 2006-02-07 2007-08-16 Tepha, Inc. Toughened polylactic acid polymers and copolymers
ES2624589T3 (es) * 2006-02-07 2017-07-17 Tepha, Inc. Métodos y dispositivos para la reparación del manguito de los rotadores
US9592325B2 (en) * 2006-02-07 2017-03-14 Tepha, Inc. Polymeric, degradable drug-eluting stents and coatings
WO2007115125A2 (en) 2006-03-31 2007-10-11 Nmt Medical, Inc. Deformable flap catch mechanism for occluder device
US8551135B2 (en) 2006-03-31 2013-10-08 W.L. Gore & Associates, Inc. Screw catch mechanism for PFO occluder and method of use
US8870913B2 (en) 2006-03-31 2014-10-28 W.L. Gore & Associates, Inc. Catch system with locking cap for patent foramen ovale (PFO) occluder
US9089627B2 (en) 2006-07-11 2015-07-28 Abbott Cardiovascular Systems Inc. Stent fabricated from polymer composite toughened by a dispersed phase
US20080082083A1 (en) * 2006-09-28 2008-04-03 Forde Sean T Perforated expandable implant recovery sheath
WO2008062995A1 (en) * 2006-11-21 2008-05-29 Lg Chem, Ltd. Copolymer comprising 4-hydroxybutyrate unit and lactate unit and its manufacturing method
US7943683B2 (en) 2006-12-01 2011-05-17 Tepha, Inc. Medical devices containing oriented films of poly-4-hydroxybutyrate and copolymers
JP2010517638A (ja) * 2007-02-02 2010-05-27 トアニエ, インコーポレイテッド 腱および靱帯を修復するシステムおよび方法
US9005242B2 (en) 2007-04-05 2015-04-14 W.L. Gore & Associates, Inc. Septal closure device with centering mechanism
WO2008131167A1 (en) 2007-04-18 2008-10-30 Nmt Medical, Inc. Flexible catheter system
US7947483B2 (en) 2007-08-10 2011-05-24 Genomatica, Inc. Methods and organisms for the growth-coupled production of 1,4-butanediol
US8581040B2 (en) 2007-08-30 2013-11-12 Plant Sensory Systems, Llc Methods of producing GABA
US8581041B2 (en) 2007-08-30 2013-11-12 Plant Sensory Systems, Llc Methods of producing GABA
AU2008296450A1 (en) * 2007-08-30 2009-03-12 Plant Sensory System, Llc. Alternative methods for the biosynthesis of GABA
TWI356705B (en) * 2007-10-25 2012-01-21 Internat Chlorella Co Ltd Extracts from chlorella sorokiniana
SG186646A1 (en) * 2007-12-13 2013-01-30 Glycos Biotechnologies Inc Microbial conversion of oils and fatty acids to high-value chemicals
US8287909B2 (en) * 2007-12-19 2012-10-16 Tepha, Inc. Medical devices containing melt-blown non-wovens of poly-4-hydroxybutyrate and copolymers thereof
KR20090078925A (ko) * 2008-01-16 2009-07-21 주식회사 엘지화학 폴리락테이트 또는 그 공중합체 생성능을 가지는 재조합미생물 및 이를 이용한 폴리락테이트 또는 그 공중합체의제조방법
US20130165967A1 (en) 2008-03-07 2013-06-27 W.L. Gore & Associates, Inc. Heart occlusion devices
US20090253154A1 (en) * 2008-04-02 2009-10-08 Immunosciences Lab., Inc. Blood and saliva test for detection of delayed food allergy and intolerance against modified foods
US8487159B2 (en) * 2008-04-28 2013-07-16 Metabolix, Inc. Production of polyhydroxybutyrate in switchgrass
CA2735883C (en) 2008-09-10 2020-05-05 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol
JP5698001B2 (ja) * 2009-02-10 2015-04-08 協和発酵バイオ株式会社 アミノ酸の製造法
CA2754108A1 (en) * 2009-03-05 2010-09-10 Metabolix, Inc. Propagation of transgenic plants
LT2438036T (lt) 2009-06-04 2017-06-26 Genomatica, Inc. Fermentacijos sultinio komponentų išskyrimo būdas
US20120029556A1 (en) 2009-06-22 2012-02-02 Masters Steven J Sealing device and delivery system
US8956389B2 (en) 2009-06-22 2015-02-17 W. L. Gore & Associates, Inc. Sealing device and delivery system
WO2011031566A1 (en) 2009-08-27 2011-03-17 Newlight Technologies, Llc Process for the production of polyhydroxyalkanoates
US9181559B2 (en) 2009-09-15 2015-11-10 Metabolix, Inc. Generation of high polyhydroxybutyrate producing oilseeds
AU2010306785B2 (en) * 2009-10-13 2016-01-14 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol, 4-hydroxybutanal, 4-hydroxybutyryl-CoA, putrescine and related compounds, and methods related thereto
WO2011063363A2 (en) * 2009-11-20 2011-05-26 Opx Biotechnologies, Inc. Production of an organic acid and/or related chemicals
US20110166598A1 (en) * 2009-12-02 2011-07-07 Entrigue Surgical, Inc. Devices and methods for tongue stabilization
US8048661B2 (en) 2010-02-23 2011-11-01 Genomatica, Inc. Microbial organisms comprising exogenous nucleic acids encoding reductive TCA pathway enzymes
US8637286B2 (en) 2010-02-23 2014-01-28 Genomatica, Inc. Methods for increasing product yields
GB2478588A (en) * 2010-03-12 2011-09-14 G5 Internat Holdings Pte Ltd Microbial production of polyhydroxyalkanoates (PHAs) using culture medium containing hydrogen
PT2558133T (pt) 2010-03-26 2020-04-23 Tepha Inc Revestimentos para o fabrico e aplicação de dispositivos médicos de polihidroxialcanqato
ES2523928T3 (es) 2010-06-15 2014-12-02 Tepha, Inc. Dispositivos médicos que contienen no-tejidos hilados en seco de poli-4-hidroxibutirato y copolímeros
US9511169B2 (en) 2010-06-15 2016-12-06 Tepha, Inc. Medical devices containing dry spun non-wovens of poly-4-hydroxybutyrate and copolymers with anisotropic properties
EP2425865A1 (en) 2010-08-06 2012-03-07 Aesculap AG Medicinal thread having a polyhydroxyalkanoate coating
WO2012037324A2 (en) 2010-09-15 2012-03-22 Metabolix, Inc. Increasing carbon flow for polyhydroxybutyrate production in biomass crops
ES2644478T3 (es) 2010-11-09 2017-11-29 Tepha, Inc. Implantes cocleares liberadores de fármacos
US8956835B2 (en) 2010-11-24 2015-02-17 Suny Research Foundation Methods for producing polyhydroxyalkanoates from biodiesel-glycerol
US9078634B2 (en) 2011-01-27 2015-07-14 Cryosa, Llc Apparatus and methods for treatment of obstructive sleep apnea utilizing cryolysis of adipose tissues
WO2012122343A2 (en) 2011-03-08 2012-09-13 Newlight Technologies, Llc Polyhydroxyalkanoate production method
EP2702091B1 (en) 2011-04-29 2019-02-13 CJ CheilJedang Corporation Process for latex production by melt emulsification
WO2012170793A1 (en) 2011-06-08 2012-12-13 Metabolix, Inc. Biorefinery process for thf production
MY165731A (en) 2011-07-29 2018-04-20 Mitsui Chemicals Inc Microorganism having carbon dioxide fixation cycle introduced thereinto
US20140170714A1 (en) 2011-08-10 2014-06-19 Metabolix, Inc. Post process purification for gamma-butyrolactone production
US9770232B2 (en) 2011-08-12 2017-09-26 W. L. Gore & Associates, Inc. Heart occlusion devices
EP3266806A1 (en) 2011-09-27 2018-01-10 Tepha, Inc. A method of making an article comrising poly-4-hydroxybutyrate or a copolymer thereof
US8940509B2 (en) 2011-11-02 2015-01-27 Genomatica, Inc. Microorganisms and methods for the production of caprolactone
US12060597B2 (en) 2011-12-02 2024-08-13 Newlight Technologies, Inc. Polyhydroxyalkanoate production methods and systems for same
US20200347417A1 (en) 2012-03-29 2020-11-05 Newlight Technologies, Inc Polyhydroxyalkanoate production methods and materials and microorganisms used in same
US9085784B1 (en) 2012-03-29 2015-07-21 Newlight Technologies, Llc Polyhydroxyalkanoate production methods and materials and microorganisms used in same
EP3238751B1 (en) 2012-05-21 2020-07-08 Tepha, Inc. Resorbable bioceramic compositions of poly-4-hydroxybutyrate and copolymers
WO2014028943A1 (en) 2012-08-17 2014-02-20 Metabolix, Inc. Biobased rubber modifiers for polymer blends
WO2014058655A1 (en) 2012-10-10 2014-04-17 Metabolix Polyhydroxyalkanoate copolymer compositions and methods of making the same
US20160068463A1 (en) 2012-11-14 2016-03-10 Metabolix, Inc. Production of salts of 4-hydroxybutyrate using biobased raw materials
US10149923B2 (en) 2013-01-15 2018-12-11 Tepha, Inc. Implants for soft and hard tissue regeneration
US10828019B2 (en) 2013-01-18 2020-11-10 W.L. Gore & Associates, Inc. Sealing device and delivery system
MY172023A (en) 2013-01-24 2019-11-12 Mitsui Chemicals Inc Microorganism having carbon dioxide fixation cycle introduced thereinto
WO2014127053A2 (en) 2013-02-13 2014-08-21 Metabolix, Inc. Process for ultra pure chemical production from biobased raw starting materials
US10201640B2 (en) 2013-03-13 2019-02-12 Tepha, Inc. Ultrafine electrospun fibers of poly-4-hydroxybutyrate and copolymers thereof
WO2015026964A1 (en) 2013-08-20 2015-02-26 Tepha, Inc. Closed cell foams including poly-4-hydroxybutyrate and copolymers thereof
US9687585B2 (en) 2013-08-20 2017-06-27 Tepha, Inc. Thermoformed poly-4-hydroxybutyrate medical implants
US9302029B2 (en) 2013-10-31 2016-04-05 Tepha, Inc. Pultrusion of poly-4-hydroxybutyrate and copolymers thereof
US9480780B2 (en) 2013-11-05 2016-11-01 Tepha, Inc. Compositions and devices of poly-4-hydroxybutyrate
US10485535B2 (en) 2013-12-19 2019-11-26 Tornier, Inc. High-strength bioabsorbable suture
EP3086820B1 (en) 2013-12-26 2020-10-28 Tepha, Inc. Medical implants including laminates of poly-4-hydroxybutyrate and copolymers thereof
US9457127B2 (en) 2014-03-18 2016-10-04 Tepha, Inc. Micro-fiber webs of poly-4-hydroxybutyrate and copolymers thereof produced by centrifugal spinning
EP3137015B1 (en) 2014-04-30 2022-01-26 Tepha, Inc. Three-dimensional resorbable implants for tissue reinforcement and hernia repair
EP3142716B1 (en) 2014-05-16 2018-04-25 Tepha, Inc. Medical devices containing dry spun non-wovens of poly-4-hydroxybutyrate and copolymers with anisotropic properties
US9808230B2 (en) 2014-06-06 2017-11-07 W. L. Gore & Associates, Inc. Sealing device and delivery system
EP3183012B1 (en) 2014-08-20 2017-12-20 Tepha, Inc. Thermoformed poly-4-hydroxybutyrate medical implants
EP3197512B1 (en) 2014-09-22 2020-05-06 Tepha, Inc. Oriented p4hb implants containing antimicrobial agents
EP3200736B8 (en) 2014-10-01 2020-06-17 CryOSA, Inc. Apparatus for treatment of obstructive sleep apnea utilizing cryolysis of adipose tissues
US20190023632A1 (en) 2016-01-06 2019-01-24 Archer Daniels Midland Company Process for producing 1,3-butanediol and for optionally further producing (r)-3-hydroxybutyl (r)-3-hydroxybutyrate
KR101774431B1 (ko) * 2016-01-28 2017-09-05 한국과학기술원 자일로즈로부터 폴리(락테이트-co-글라이콜레이트) 또는 그 공중합체 생산능을 가지는 재조합 미생물 및 이를 이용한 폴리(락테이트-co-글라이콜레이트) 또는 그 공중합체의 제조방법
WO2018217574A1 (en) 2017-05-25 2018-11-29 Tepha, Inc. Continuous formation of tubes of poly-4-hydroxybutyrate and copolymers thereof
CN109112151B (zh) * 2017-06-23 2021-10-29 北京蓝晶微生物科技有限公司 一种精细调控共聚物中4-羟基丁酸组成比例的基因盒及其应用
WO2019050936A1 (en) 2017-09-06 2019-03-14 Tepha, Inc. CALANDERATED SURGICAL TRELLIS COMPRISING POLYHYDROXYALKANOATES
ES2916298T3 (es) 2017-12-04 2022-06-29 Tepha Inc Implantes médicos de poli-4-hidroxibutirato termoformado con membrana al vacío
CA3102277C (en) 2018-06-11 2024-11-12 Tepha Inc PROCESSES FOR 3D PRINTING POLY-4-HYDROXYBUTYRATE AND COPOLYMERS
ES2956815T3 (es) 2018-10-29 2023-12-28 Tepha Inc Procedimientos de fabricación de suturas de malla a partir de poli-4-hidroxibutirato y sus copolímeros
TWI827804B (zh) * 2019-03-06 2024-01-01 日商三菱商事生命科學股份有限公司 蕈菌絲體之製造方法、含有蕈菌絲體的組成物、以及使用了蕈菌絲體之食品材料
AU2020293986A1 (en) 2019-06-10 2022-01-06 Nuseed Nutritional Us Inc. Transgenic land plants that express a polyhydroxyalkanoate synthase seed specifically with cytosolic localization
FR3109290B1 (fr) 2020-04-17 2025-04-11 Ph Tech Dispositif médical comprenant une matrice biologique acellulaire et au moins un polymère
FR3110077B1 (fr) 2020-05-12 2024-12-06 Ph Tech Procédé de fabrication d’un dispositif médical en trois dimensions et dispositif médical obtenu
FR3113371A1 (fr) 2020-08-12 2022-02-18 Ph Tech Dispositif médical comprenant un assemblage d’éléments de matrices biologiques acellulaires et au moins un polymère
WO2022192168A1 (en) 2021-03-11 2022-09-15 Tepha, Inc. Breast reconstruction implant
WO2023130069A2 (en) 2021-12-30 2023-07-06 Cryosa, Inc. Systems and methods for treatment of obstructive sleep apnea
AU2023354862A1 (en) * 2022-09-30 2025-05-01 Kimberly-Clark Worldwide, Inc. In vitro bioproduction of specific chain length poly(hydroxyalkanoate) monomers

Family Cites Families (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS575693A (en) 1980-06-13 1982-01-12 Ajinomoto Co Inc Production of l-arginine through fermentation process
IE50442B1 (en) * 1980-11-21 1986-04-16 Loctite Corp Two part adhesive composition
US5250430A (en) 1987-06-29 1993-10-05 Massachusetts Institute Of Technology Polyhydroxyalkanoate polymerase
US5245023A (en) 1987-06-29 1993-09-14 Massachusetts Institute Of Technology Method for producing novel polyester biopolymers
US4876331A (en) 1987-08-18 1989-10-24 Mitsubishi Kasei Corporation Copolyester and process for producing the same
US4876831A (en) * 1988-03-14 1989-10-31 Runyon John F Folding modular building structure
US5004664A (en) 1989-02-27 1991-04-02 Xerox Corporation Toner and developer compositions containing biodegradable semicrystalline polyesters
US5371002A (en) 1989-06-07 1994-12-06 James Madison University Method of production of poly-beta-hydroxyalkanoate copolymers
ES2131489T3 (es) 1989-07-10 2003-05-16 Massachusetts Inst Technology Una planta o una celula vegetal recombinante capaz de producir polihidroxibutirato u otro polihidroxialcanoato.
IE893328A1 (en) 1989-10-16 1991-04-24 Mcdaid Denis Telephone lock
GB9108756D0 (en) 1991-04-24 1991-06-12 Ici Plc Production of polyalkanoate in plants
US5286842A (en) 1991-07-01 1994-02-15 Mitsubishi Kasei Corporation Process for producing a biodegradable polymer
GB9115245D0 (en) 1991-07-16 1991-08-28 Ici Plc Production of polyalkanoate
CA2113412C (en) 1991-07-19 2000-01-25 Christopher R. Somerville Transgenic plants producing polyhydroxyalkanoates
US5610041A (en) 1991-07-19 1997-03-11 Board Of Trustees Operating Michigan State University Processes for producing polyhydroxybutyrate and related polyhydroxyalkanoates in the plastids of higher plants
PH30131A (en) 1991-08-07 1997-01-21 Ajinomoto Kk Process for producing l-glutamic acid by fermentation
JP2777757B2 (ja) 1991-09-17 1998-07-23 鐘淵化学工業株式会社 共重合体およびその製造方法
GB9223332D0 (en) * 1992-11-06 1992-12-23 Ici Plc Production of polyhydroxyalkanoate in plants
WO1994012014A1 (en) 1992-11-20 1994-06-09 Agracetus, Inc. Transgenic cotton plants producing heterologous bioplastic
JP3263710B2 (ja) 1992-12-11 2002-03-11 高砂香料工業株式会社 生分解性光学活性ポリマー及びその製造方法
US6849427B1 (en) 1993-03-12 2005-02-01 Immulogic Pharmaceutical Corp. Nucleic acids encoding a house dust mite allergen, Der p VII, and uses therefor
IL108947A0 (en) 1993-03-12 1994-06-24 Osteopharm Ltd Bone stimulating factor
JP3241505B2 (ja) 1993-08-11 2001-12-25 高砂香料工業株式会社 生分解性光学活性コポリマー及びその製造方法
ID23491A (id) 1994-01-28 1995-09-07 Procter & Gamble Kopolimer-kopolimer yang dapat dibiodegradasi dan baha-bahan plastik yang terdiri dari kopolimer-kopolimer yang dapat dibiodegradasi
BR9506664A (pt) 1994-01-28 1997-09-16 Procter & Gamble Copolímeros biodegradâveis e artigos plásticos compreendendo copolímeros biodegradâveis de 3-hidroxihexanoato
CA2125313A1 (en) * 1994-06-07 1995-12-08 Gerald E. O'grady Method and apparatus for producing electrical energy within the body of a ruminant
US5563239A (en) 1994-11-09 1996-10-08 Eastman Chemical Company Composition and process for the production of poly(3-hydroxyalkanoates)
BE1008983A6 (fr) 1994-12-30 1996-10-01 Faco Sa Bigoudi.
US5763270A (en) 1995-06-07 1998-06-09 Genemedicine, Inc. Plasmid for delivery of nucleic acids to cells and methods of use
GB9602796D0 (en) * 1996-02-12 1996-04-10 Innes John Centre Innov Ltd Genetic control of plant growth and development
US6117658A (en) * 1997-02-13 2000-09-12 James Madison University Methods of making polyhydroxyalkanoates comprising 4-hydroxybutyrate monomer units

Cited By (72)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999061624A3 (en) * 1998-05-22 2000-02-17 Metabolix Inc Polyhydroxyalkanoate biopolymer compositions
US7202064B2 (en) 1998-05-22 2007-04-10 Metabolix, Inc. Polyhydroxyalkanoate biopolymer compositions
US6323010B1 (en) 1998-05-22 2001-11-27 Metabolix, Inc. Polyhydroxyalkanoate biopolymer compositions
US8093022B2 (en) 1998-05-22 2012-01-10 Metabolix, Inc. Polyhydroxyalkanoate biopolymer compositions
US8609378B2 (en) 1998-08-04 2013-12-17 Metabolix, Inc. Polyhydroxyalkanoate production from polyols
EP1975236A2 (en) 1998-08-04 2008-10-01 Metabolix, Inc. Polyhydroxyalkanoate production from polyols
US6329183B1 (en) 1998-08-04 2001-12-11 Metabolix, Inc. Polyhydroxyalkanoate production from polyols
US8114643B2 (en) 1998-08-04 2012-02-14 Metabolix, Inc. Polyhydroxyalkanoate production from polyols
US6576450B2 (en) 1998-08-04 2003-06-10 Metabolix, Inc. Polyhydroxyalkanoate production from polyols
AU753132B2 (en) * 1998-08-18 2002-10-10 Metabolix, Inc. Transgenic microbial polyhydroxyalkanoate producers
US6913911B2 (en) 1998-08-18 2005-07-05 Metabolix, Inc. Transgenic microbial polyhydroxyalkanoate producers
US6593116B1 (en) 1998-08-18 2003-07-15 Metabolix, Inc. Transgenic microbial polyhydroxyalkanoate producers
WO2000011188A1 (en) * 1998-08-18 2000-03-02 Metabolix, Inc. Transgenic microbial polyhydroxyalkanoate producers
EP1700908A3 (en) * 1998-08-18 2008-10-29 Metabolix, Inc. Transgenic microbial polyhydroxyalkanoate producers
EP1700909A3 (en) * 1998-08-18 2007-12-05 Metabolix, Inc. Transgenic microbial polyhydroxyalkanoate producers
US6623730B1 (en) 1999-09-14 2003-09-23 Tepha, Inc. Therapeutic uses of polymers and oligomers comprising gamma-hydroxybutyrate
US8293971B2 (en) 2000-02-11 2012-10-23 Metabolix, Inc. Multi-gene expression constructs containing modified inteins
US7026526B2 (en) 2000-02-11 2006-04-11 Metabolix, Inc. Multi-gene expression constructs containing modified inteins
US7741530B2 (en) 2000-02-11 2010-06-22 Metabolix, Inc. Multi-gene expression constructs containing modified inteins
US8741624B2 (en) 2000-07-21 2014-06-03 Metabolix, Inc. Production of polyhydroxyalkanoates from polyols
US6897338B2 (en) 2001-12-18 2005-05-24 Metabolix, Inc. Methods of making intermediates from polyhydroxyalkanoates
US7166743B2 (en) 2001-12-18 2007-01-23 Metabolix, Inc. Methods of making intermediates from polyhydroxyalkanoates
US6844447B2 (en) 2001-12-18 2005-01-18 Metabolix Inc. Methods of making intermediates from polyhydroxyalkanoates
US6933404B2 (en) 2001-12-18 2005-08-23 Metabolix Inc. Methods of making intermediates from polyhydroxyalkanoates
US7001969B2 (en) 2001-12-18 2006-02-21 Metabolix Inc. Methods of making intermediates from polyhydroxyalkanoates
US7230144B2 (en) 2001-12-18 2007-06-12 Metabolix Inc. Methods of making intermediates from polyhydroxyalkanoates
WO2004024876A2 (en) 2002-09-12 2004-03-25 Metabolix, Inc. Polyhydroxyalkanoate production by coenzyme a-dependent aldehyde dehydrogenase pathways
EP2365088A2 (en) 2002-09-12 2011-09-14 Metalbolix Inc. Polyhydroxyalkanoate production by coenzyme a-dependent aldehyde dehydrogenase pathways
US8071355B2 (en) 2002-09-12 2011-12-06 Metabolix, Inc. Polyhydroxyalkanoate production by coenzyme A-dependent aldehyde dehydrogenase pathways
WO2004065609A1 (ja) 2003-01-22 2004-08-05 Showa Denko K.K. アシルコエンザイムaを用いるアシル基転移酵素反応方法
US7943351B2 (en) 2003-01-22 2011-05-17 Showa Denko K.K. Method for acyltransferase reaction using acyl coenzyme A
US7476521B2 (en) 2003-01-22 2009-01-13 Showa Denko K.K. Method for acyltransferase reaction using acyl coenzyme A
US10314683B2 (en) 2003-05-08 2019-06-11 Tepha, Inc. Polyhydroxyalkanoate medical textiles and fibers
US10136982B2 (en) 2003-05-08 2018-11-27 Tepha, Inc. Polyhydroxyalkanoate medical textiles and fibers
US10111738B2 (en) 2003-05-08 2018-10-30 Tepha, Inc. Polyhydroxyalkanoate medical textiles and fibers
US8742203B2 (en) 2005-03-16 2014-06-03 Metabolix, Inc. Chemically Inducible Expression of Biosynthetic Pathways
US7732680B2 (en) 2005-03-16 2010-06-08 Metabolix, Inc. Chemically inducible expression of biosynthetic pathways
EP2048224A4 (en) * 2006-07-21 2009-12-16 Kaneka Corp MICROORGANISM WITH EXCHANGED GENE AND METHOD FOR PRODUCING POLYESTER THEREWITH
EP3800262A1 (en) * 2007-03-16 2021-04-07 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
US11371046B2 (en) 2007-03-16 2022-06-28 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
EP2821494A1 (en) * 2007-03-16 2015-01-07 Genomatica, Inc. Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
CN105936887A (zh) * 2007-03-16 2016-09-14 基因组股份公司 用于1,4-丁二醇和其前体生物合成的组合物和方法
WO2008115840A3 (en) * 2007-03-16 2009-01-29 Genomatica Inc Compositions and methods for the biosynthesis of 1,4-butanediol and its precursors
TWI568847B (zh) * 2007-03-16 2017-02-01 奇諾麥提卡公司 用於1,4-丁二醇及其前驅物之生物合成的組合物及方法
WO2010006076A3 (en) * 2008-07-08 2010-07-29 Opx Biotechnologies Inc. Methods, compositions and systems for biosynthetic bio production of 1,4-butanediol
CN103396978A (zh) * 2008-12-12 2013-11-20 麦特波力克斯公司 用于制备聚(5-羟基戊酸)和5碳化合物的绿色工艺和组合物
US9090898B2 (en) 2008-12-12 2015-07-28 Metabolix, Inc. Green process and compositions for producing poly(5HV) and 5 carbon chemicals
US10273508B2 (en) 2009-06-04 2019-04-30 Genomatica, Inc. Microorganisms for the production of 1,4-butanediol and related methods
US11401534B2 (en) 2009-06-04 2022-08-02 Genomatica, Inc. Microorganisms for the production of 1,4- butanediol and related methods
US10662451B2 (en) 2009-11-25 2020-05-26 Genomatica, Inc. Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US9988656B2 (en) 2009-11-25 2018-06-05 Genomatica, Inc. Microorganisms and methods for the coproduction 1,4-butanediol and gamma-butyrolactone
US10786064B2 (en) 2010-02-11 2020-09-29 Cj Cheiljedang Corporation Process for producing a monomer component from a genetically modified polyhydroxyalkanoate biomass
WO2012149162A3 (en) * 2011-04-29 2013-01-17 Metabolix, Inc. Green process for producing polyhydroxyalkanoates and chemicals using a renewable feedstock
US9663791B2 (en) 2011-04-29 2017-05-30 Cj Research Center Llc Green process for producing polyhydroxyalkanoates and chemicals using a renewable feedstock
US9447441B2 (en) 2011-09-05 2016-09-20 Riken Method for producing polyhydroxyalkanoate having long main chain structure
WO2013062977A1 (en) 2011-10-25 2013-05-02 Marrone Bio Innovations, Inc. Chromobacterium formulations, compostions, metabolites and their uses
CN104520433A (zh) * 2012-04-11 2015-04-15 赫姆霍尔兹传染病研究中心有限责任公司 产生pha的基因工程微生物
WO2013153180A1 (en) * 2012-04-11 2013-10-17 Helmholtz-Zentrum für Infektionsforschung GmbH Pha-producing genetically engineered microorganisms
US11932845B2 (en) 2012-06-04 2024-03-19 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds
US9677045B2 (en) 2012-06-04 2017-06-13 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds
US11085015B2 (en) 2012-06-04 2021-08-10 Genomatica, Inc. Microorganisms and methods for production of 4-hydroxybutyrate, 1,4-butanediol and related compounds
US9850192B2 (en) 2012-06-08 2017-12-26 Cj Cheiljedang Corporation Renewable acrylic acid production and products made therefrom
US11426484B2 (en) 2014-08-15 2022-08-30 Tepha, Inc. Self-retaining sutures of poly-4-hydroxybutyrate and copolymers thereof
US10500303B2 (en) 2014-08-15 2019-12-10 Tepha, Inc. Self-retaining sutures of poly-4-hydroxybutyrate and copolymers thereof
US11944709B2 (en) 2014-08-15 2024-04-02 Tepha, Inc. Self-retaining sutures of poly-4-hydroxybutyrate and copolymers thereof
US10626521B2 (en) 2014-12-11 2020-04-21 Tepha, Inc. Methods of manufacturing mesh sutures from poly-4-hydroxybutyrate and copolymers thereof
US10590566B2 (en) 2014-12-11 2020-03-17 Tepha, Inc. Methods of orienting multifilament yarn and monofilaments of poly-4-hydroxybutyrate and copolymers thereof
US11828006B2 (en) 2014-12-11 2023-11-28 Tepha, Inc. Methods of orienting multifilament yarn and monofilaments of poly-4-hydroxybutyrate and copolymers thereof
US10227713B2 (en) 2014-12-11 2019-03-12 Tepha, Inc. Methods of orienting multifilament yarn and monofilaments of poly-4-hydroxybutyrate and copolymers thereof
US10801050B2 (en) 2015-10-23 2020-10-13 Metabolic Explorer Microorganism modified for the assimilation of levulinic acid
CN113832084A (zh) * 2021-09-29 2021-12-24 北京化工大学 一种生产聚羟基脂肪酸酯的溶藻弧菌及其应用
CN113832084B (zh) * 2021-09-29 2024-01-05 北京化工大学 一种生产聚羟基脂肪酸酯的溶藻弧菌及其应用

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US7229804B2 (en) 2007-06-12
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US20060084155A1 (en) 2006-04-20
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