Methods for producing poly(hydroxy) fatty acids in bacteria
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IPC분류정보
국가/구분
United States(US) Patent
등록
국제특허분류(IPC7판)
C12P-007/64
C12P-021/06
C12P-001/00
C12N-001/20
C07H-021/04
출원번호
US-0779427
(2001-02-08)
우선권정보
DE-44 33 134 (1994-09-16)
발명자
/ 주소
Steinbü
chel, Alexander
Liebergesell, Mathias
Valentin, Henry
Pries, Andreas
출원인 / 주소
Metabolix, Inc.
대리인 / 주소
Pabst Patent Group LLP
인용정보
피인용 횟수 :
38인용 특허 :
0
초록▼
The present invention relates to a process for the production of poly (hydroxy fatty acids) as well as recombinant bacterial strains for carrying out the process. In addition, new poly(hydroxy fatty acids) and new substrates for the production of conventional and new poly(hydroxy fatty acids) are de
The present invention relates to a process for the production of poly (hydroxy fatty acids) as well as recombinant bacterial strains for carrying out the process. In addition, new poly(hydroxy fatty acids) and new substrates for the production of conventional and new poly(hydroxy fatty acids) are described. Moreover, the invention also relates to a DNA fragment, which codes for a PhaE and a PhaC component of the poly(hydroxy fatty acid) synthase from Thiocapsa pfennigii , as well as the corresponding poly (hydroxy fatty acid) synthase protein.
대표청구항▼
1. A process for the preparation of poly(hydroxy fatty acids) comprising incubating a recombinant bacteria in a mineral medium under aerobic conditions, expressing at least one fragment of the gene encoding the poly(hydroxy fatty acid) synthase from Thiocapsa pfennigii with a substrate carbon sourc
1. A process for the preparation of poly(hydroxy fatty acids) comprising incubating a recombinant bacteria in a mineral medium under aerobic conditions, expressing at least one fragment of the gene encoding the poly(hydroxy fatty acid) synthase from Thiocapsa pfennigii with a substrate carbon source, wherein the recombinant organism produces a poly(hydroxy fatty acid) and, the poly(hydroxy fatty acid) are recovered. 2. The process of claim 1, wherein the bacteria are pre-cultivated in a complex medium. 3. The process of claim 1, wherein one also adds to the bacterial culture at least one additional carbon source which promotes growth, whereby the carbon source is selected from the group consisting ofcitric acid, citric acid salts, citric acid esters, citric acid lactones, octanoic acid, octanoic acid salts, octanoic acid esters, octanoic acid lactones, gluconic acid, gluconic acid salts, gluconic acid esters, gluconic acid lactones, hexoses, and combinations thereof. 4. The process of claim 1, wherein the process is carried out in the form of a batch process, a fed-batch process, a two-step process or a continuous flow process. 5. The process of claim 1, wherein the poly(hydroxy fatty acids) are obtained in a concentration of approximately 15 to 70% by weight based on the dry mass of the bacterial cells. 6. The process of claim 1, wherein the poly(hydroxy fatty acids) are obtained in the form of copolyesters with at least two subunits. 7. The process of claim 1, wherein the recombinant bacteria are incubated at cell densities of up to 100 g of dry cellular mass per liter of bacterial nutrient medium. 8. The process of claim 1, wherein one offers the substrate carbon source in excess. 9. The process of claim 8, wherein one offers the substrate carbon source at a concentration of approximately 0.1 to 5% by weight. 10. The process of claim 9, wherein one increases the concentration of the substrate carbon source in the culture medium in steps, optionally with pre-incubation in the presence of in additional carbon source which does not serve as a substrate. 11. The process of claim 10, wherein, one adds approximately 0.5% (weight/volume) of neutralized substrate carbon source after approximately 12 hours and 24 hours of pre-incubation at approximately 27° C. to 35° C. 12. The process of claim 1, wherein incubation takes place for approximately 24 h to 96 h. 13. The process of claim 1, wherein the recombinant bacteria are cultivated under conditions deficient in an element wherein the element is selected from the group consisting of nitrogen, magnesium or phosphate. 14. The process of claim 1, wherein the recombinant bacteria are harvested and are broken open in order to obtain the poly(hydroxy fatty acids) that have been produced. 15. The process of claim 14, wherein the harvested recombinant bacteria are lyophilized and then extracted with an organic solvent, selected from the group consisting of chloroform or methylene chloride, in order to break open the recombinant bacteria and to obtain the poly(hydroxy fatty acids). 16. The process of claim 15, wherein the extracted poly(hydroxy fatty acid) produced is precipitated by introducing a hydrophilic solvent, selected from the group consisting of water and a lower alcohol, wherein the product is obtained by removing the hydrophilic solvent. 17. The process of claim 14, wherein the harvested recombinant bacteria are broken open by means selected from the group consisting of detergents, a lytic enzyme cocktail, and a combination thereof wherein the bacterial cell grana, which contain the poly(hydroxy fatty acids), are collected. 18. The process of claim 17, wherein the lytic enzyme cocktail contains enzymes which are selected from the group consisting of lysozyme; proteases; other hydrolytic enzymes; and combinations thereof. 19. The process of claim 1, wherein the poly(hydroxy fatty acids) are obtained in a concentration of approximately 15 to 50% by weight based on the dry mass of the bacterial cells. 20. The process of claim 1, wherein the poly(hydroxy fatty acids) are obtained in a concentration of approximately 40% by weight based on the dry mass of the bacterial cells. 21. The process of claim 1, wherein one adds approximately 0.5% (weight/volume) of neutralized substrate carbon source at each step, after approximately 12 hours and 24 hours of incubation at approximately 30° C. 22. The process of claim 1, wherein incubation takes place for approximately 36 hours to 72 hours. 23. The process of claim 1, wherein incubation takes place for approximately 48 hours to 72 hours. 24. The process of claim 1 wherein the poly(hydroxy fatty acids) are comprised of one or more combinations of monomers selected from the group consisting of:3-hydroxybutyric acid, 3 hydroxyvaleric acid and 4-hydroxy-valeric acid;3-hydroxybutyric acid, 3 hydroxyvaleric acid, 4-hydroxy-valeric acid, 3-hydroxyhexanoic acid and 3-hydroxyoctanoic acid;3-hydroxybutyric acid, 3-hydroxyhexanoic acid, 5-hydroxyhexanoic acid, and 3-hydroxyoctanoic acid;3-hydroxybutyric meld, 3 hydroxyvaleric acid, 3-hydroxyhexanoic acid, 3-hydroxyheptanoic acid, 4-hydroxyheptanoic acid and 3-hydroxyoctanoic acid;3-hydroxybutyric acid, 3 hydroxyhexanoic acid, 3-hydroxy-octanoic acid and 4-hydroxyoctanoic acid;3-hydroxybutyric acid, 3-hydroxyhexanoic acid and 5-hydroxyheptanoic acid;3-hydroxybutyric acid, 3-hydroxyvaleric acid, 3-hydroxy-heptanoic acid and 4-hydroxyheptanoic acid;3-hydroxybutyric acid, 3 hydroxyvaleric acid, 3-hydroxyhexanoic acid, 3-hydroxyoctanoic acid, and 4-hydroxyoctanoic acid;3-hydroxybutyric acid, 3-hydroxyhexanoic acid and 4-hydroxyhexanoic acid; and3-hydroxybutyric acid, and 5-hydroxyhexanoic acid.
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