WO2011090493A1 - Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof - Google Patents

Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof Download PDF

Info

Publication number
WO2011090493A1
WO2011090493A1 PCT/US2010/028175 US2010028175W WO2011090493A1 WO 2011090493 A1 WO2011090493 A1 WO 2011090493A1 US 2010028175 W US2010028175 W US 2010028175W WO 2011090493 A1 WO2011090493 A1 WO 2011090493A1
Authority
WO
WIPO (PCT)
Prior art keywords
pta
isolated
biomass
weight
acid
Prior art date
Application number
PCT/US2010/028175
Other languages
French (fr)
Inventor
Kirk E. Apt
Paul Warren Behrens
Jon Milton Hansen
Joseph W. PFEIFER III
Tracey Lynn Stahl
Ross Zirkle
Original Assignee
Martek Biosciences Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=44277725&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO2011090493(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority to KR1020147033815A priority Critical patent/KR20150013667A/en
Priority to KR1020127021791A priority patent/KR20120133381A/en
Priority to KR1020187025169A priority patent/KR102447978B1/en
Priority to EA201290656A priority patent/EA031136B1/en
Priority to EP21196529.8A priority patent/EP4056708A1/en
Priority to CA2787344A priority patent/CA2787344C/en
Priority to DK10844116.3T priority patent/DK2526197T3/en
Priority to EP10844116.3A priority patent/EP2526197B1/en
Priority to CN201080062727.2A priority patent/CN102884201B/en
Priority to BR122015020119A priority patent/BR122015020119B8/en
Priority to NZ601757A priority patent/NZ601757A/en
Priority to JP2012549979A priority patent/JP5920890B2/en
Priority to AU2010343305A priority patent/AU2010343305B2/en
Priority to MX2012008388A priority patent/MX343403B/en
Priority to BR112012017831A priority patent/BR112012017831B8/en
Priority to KR1020177024272A priority patent/KR102155409B1/en
Application filed by Martek Biosciences Corporation filed Critical Martek Biosciences Corporation
Publication of WO2011090493A1 publication Critical patent/WO2011090493A1/en
Priority to PH12016501930A priority patent/PH12016501930B1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/12—Unicellular algae; Culture media therefor
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K20/00—Accessory food factors for animal feeding-stuffs
    • A23K20/10—Organic substances
    • A23K20/158—Fatty acids; Fats; Products containing oils or fats
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C9/00—Milk preparations; Milk powder or milk powder preparations
    • A23C9/152—Milk preparations; Milk powder or milk powder preparations containing additives
    • A23C9/1528—Fatty acids; Mono- or diglycerides; Petroleum jelly; Paraffine; Phospholipids; Derivatives thereof
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/007—Other edible oils or fats, e.g. shortenings, cooking oils characterised by ingredients other than fatty acid triglycerides
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K10/00—Animal feeding-stuffs
    • A23K10/10—Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A23K10/12—Animal feeding-stuffs obtained by microbiological or biochemical processes by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/40—Feeding-stuffs specially adapted for particular animals for carnivorous animals, e.g. cats or dogs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/80—Feeding-stuffs specially adapted for particular animals for aquatic animals, e.g. fish, crustaceans or molluscs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/115—Fatty acids or derivatives thereof; Fats or oils
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/40—Complete food formulations for specific consumer groups or specific purposes, e.g. infant formula
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/185—Acids; Anhydrides, halides or salts thereof, e.g. sulfur acids, imidic, hydrazonic or hydroximic acids
    • A61K31/19—Carboxylic acids, e.g. valproic acid
    • A61K31/20—Carboxylic acids, e.g. valproic acid having a carboxyl group bound to a chain of seven or more carbon atoms, e.g. stearic, palmitic, arachidic acids
    • A61K31/201—Carboxylic acids, e.g. valproic acid having a carboxyl group bound to a chain of seven or more carbon atoms, e.g. stearic, palmitic, arachidic acids having one or two double bonds, e.g. oleic, linoleic acids
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/185—Acids; Anhydrides, halides or salts thereof, e.g. sulfur acids, imidic, hydrazonic or hydroximic acids
    • A61K31/19—Carboxylic acids, e.g. valproic acid
    • A61K31/20—Carboxylic acids, e.g. valproic acid having a carboxyl group bound to a chain of seven or more carbon atoms, e.g. stearic, palmitic, arachidic acids
    • A61K31/202—Carboxylic acids, e.g. valproic acid having a carboxyl group bound to a chain of seven or more carbon atoms, e.g. stearic, palmitic, arachidic acids having three or more double bonds, e.g. linolenic
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K35/00—Medicinal preparations containing materials or reaction products thereof with undetermined constitution
    • A61K35/66—Microorganisms or materials therefrom
    • A61K35/68—Protozoa, e.g. flagella, amoebas, sporozoans, plasmodium or toxoplasma
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/33—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing oxygen
    • A61K8/36—Carboxylic acids; Salts or anhydrides thereof
    • A61K8/361—Carboxylic acids having more than seven carbon atoms in an unbroken chain; Salts or anhydrides thereof
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P29/00—Non-central analgesic, antipyretic or antiinflammatory agents, e.g. antirheumatic agents; Non-steroidal antiinflammatory drugs [NSAID]
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P3/00—Drugs for disorders of the metabolism
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P3/00—Drugs for disorders of the metabolism
    • A61P3/02—Nutrients, e.g. vitamins, minerals
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q19/00—Preparations for care of the skin
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B1/00—Production of fats or fatty oils from raw materials
    • C11B1/10—Production of fats or fatty oils from raw materials by extracting
    • C—CHEMISTRY; METALLURGY
    • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00—Refining fats or fatty oils
    • C11B3/02—Refining fats or fatty oils by chemical reaction
    • C11B3/04—Refining fats or fatty oils by chemical reaction with acids
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/10—Protozoa; Culture media therefor
    • C12N1/105—Protozoal isolates
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/12—Unicellular algae; Culture media therefor
    • C12N1/125—Unicellular algae isolates
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C12P7/6409—Fatty acids
    • C12P7/6427—Polyunsaturated fatty acids [PUFA], i.e. having two or more double bonds in their backbone
    • C12P7/6432—Eicosapentaenoic acids [EPA]
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C12P7/6409—Fatty acids
    • C12P7/6427—Polyunsaturated fatty acids [PUFA], i.e. having two or more double bonds in their backbone
    • C12P7/6434—Docosahexenoic acids [DHA]
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C12P7/6436—Fatty acid esters
    • C12P7/6445—Glycerides
    • C12P7/6458—Glycerides by transesterification, e.g. interesterification, ester interchange, alcoholysis or acidolysis
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
    • C12P7/6436—Fatty acid esters
    • C12P7/6445—Glycerides
    • C12P7/6472—Glycerides containing polyunsaturated fatty acid [PUFA] residues, i.e. having two or more double bonds in their backbone
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
    • A61K2800/10—General cosmetic use
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00—Microorganisms ; Processes using microorganisms
    • C12R2001/89—Algae ; Processes using algae
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00—Microorganisms ; Processes using microorganisms
    • C12R2001/90—Protozoa ; Processes using protozoa
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
    • Y02A40/81—Aquaculture, e.g. of fish
    • Y02A40/818—Alternative feeds for fish, e.g. in aquacultures

Definitions

  • the present invention is directed to isolated microorganisms as well as strains and mutants thereof, biomasses, microbial oils, compositions, and cultures; methods of producing the microbial oils, biomasses, and mutants; and methods of using the isolated microorganisms, biomasses, and microbial oils.
  • Fatty acids are classified based on the length and saturation characteristics of the carbon chain. Fatty acids are termed short chain, medium chain, or long chain fatty acids based on the number of carbons present in the chain, are termed saturated fatty acids when no double bonds are present between the carbon atoms, and are termed unsaturated fatty acids when double bonds are present. Unsaturated long chain fatty acids are monounsaturated when only one double bond is present and are polyunsaturated when more than one double bond is present.
  • PUFAs Polyunsaturated fatty acids
  • omega-3 (n-3) fatty acids contain a first double bond at the third carbon
  • omega-6 (n-6) fatty acids contain a first double bond at the sixth carbon.
  • docosahexaenoic acid is an omega-3 long chain polyunsaturated fatty acid (LC-PUFA) with a chain length of 22 carbons and 6 double bonds, often designated as “22:6 n-3.”
  • omega-3 LC-PUFAs include eicosapentaenoic acid (“EPA”), designated as “20:5 n-3,” and omega-3 docosapentaenoic acid (“DPA n-3”), designated as "22:5 n-3.”
  • DHA and EPA have been termed "essential” fatty acids.
  • Omega-6 LC-PUFAs include arachidonic acid (“ARA”), designated as “20:4 n-6,” and omega-6 docosapentaenoic acid (“DPA n-6”), designated as "22:5 n-6.”
  • ARA arachidonic acid
  • DPA n-6 omega-6 docosapentaenoic acid
  • Omega-3 fatty acids are biologically important molecules that affect cellular physiology due to their presence in cell membranes, regulate production and gene expression of biologically active compounds, and serve as biosynthetic substrates.
  • DHA for example, accounts for approximately 15%-20% of lipids in the human cerebral cortex, 30%-60% of lipids in the retina, is concentrated in the testes and sperm, and is an important component of breast milk. Berge, J. P., and Barnathan, G.. Adv. Biochem. Eng. Biotechnol. 9(5:49-125 (2005).
  • DHA accounts for up to 97% of the omega-3 fatty acids in the brain and up to 93% of the omega-3 fatty acids in the retina. Moreover, DHA is essential for both fetal and infant development as well as maintenance of cognitive functions in adults. Id. Because omega-3 fatty acids are not synthesized de novo in the human body, these fatty acids must be derived from nutritional sources.
  • Flaxseed oil and fish oils are considered good dietary sources of omega-3 fatty acids. Flaxseed oil contains no EPA, DHA, DPA, or ARA but rather contains linolenic acid (C I 8:3 n-3), a building block enabling the body to manufacture EPA. There is evidence, however, that the rate of metabolic conversion can be slow and variable, particularly among those with impaired health. Fish oils vary considerably in the type and level of fatty acid composition depending on the particular species and their diets. For example, fish raised by aquaculture tend to have a lower level of omega-3 fatty acids than those in the wild. Furthermore, fish oils carry the risk of containing environmental contaminants and can be associated with stability problems and a fishy odor or taste.
  • Thraustochytrids are microorganisms of the order Thraustochytriales.
  • Thraustochytrids include members of the genus Schizochytrium and Thraustochytrium and have been recognized as an alternative source of omega-3 fatty acids, including DHA and EPA. See U.S. Patent No. 5,130,242. Oils produced from these marine heterotrophic microorganisms often have simpler polyunsaturated fatty acid profiles than corresponding fish or microalgal oils. Lewis, T.E., Mar. Biotechnol. I 580-587 (1999). Strains of thraustochytrid species have been reported to produce omega-3 fatty acids as a high percentage of the total fatty acids produced by the organisms. U.S. Patent No. 5,130,242; Huang, J. et al., J. Am. Oil.
  • the present invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA- 10212.
  • the present invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA-10212.
  • the present invention is directed to an isolated microorganism comprising an 18s rRNA comprising a polynucleotide sequence of SEQ ID NO: l or a polynucleotide sequence having at least 94% identity to SEQ ID NOT .
  • the present invention is directed to an isolated microorganism comprising an 18s rRNA polynucleotide sequence that has at least 94% identity to an 18s rRNA polynucleotide sequence of the microorganism deposited under ATCC Accession No.
  • the present invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10% by weight eicosapentaenoic acid.
  • the present invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10% by weight eicosapentaenoic acid.
  • the present invention is directed to an isolated microorganism that produces a triacylglycerol fraction, wherein eicosapentaenoic acid content of the triacylglycerol fraction is at least about 12% by weight.
  • the isolated microorganism of the invention is a mutant strain.
  • the present invention is directed to an isolated microorganism deposited under
  • PTA-10212 ATCC Accession No. PTA-10212, PTA- 10213, PTA- 10214, PTA- 10215.
  • the present invention is directed to a biomass comprising any of the microorganisms of the invention or mixtures thereof. [0017] The present invention is directed to an isolated biomass, wherein at least about
  • fatty acids 20% by weight of a dry cell weight of the biomass are fatty acids, wherein more than about 10% by weight of fatty acids is eicosapentaenoic acid, and wherein the fatty acids comprise less than about 5% by weight each of arachidonic acid and docosapentaenoic acid n-6. In some embodiments, at least about 25% by weight of the fatty acids is docosahexaenoic acid.
  • the present invention is directed to an isolated biomass comprising triacylglycerol, wherein at least about 12% by weight of triacylglycerol is eicosapentaenoic acid.
  • the present invention is directed to any of the isolated biomasses of the invention wherein the fatty acids further comprise less than about 5% by weight each of oleic acid, linoleic acid, linolenic acid, eicosenoic acid, and erucic acid.
  • the present invention is directed to an isolated culture comprising any of the microorganisms of the invention or mixtures thereof.
  • the present invention is directed to a food product, cosmetic, or pharmaceutical composition for a non-human animal or human, comprising any of the microorganisms or biomasses of the invention or mixtures thereof.
  • the present invention is directed to a microbial oil comprising at least about 20% by weight eicosapentaenoic acid and less than about 5% by weight each of arachidonic acid, docosapentaenoic acid n-6, oleic acid, linoleic acid, linolenic acid, eicosenoic acid, erucic acid, and stearidonic acid.
  • the microbial oil further comprises at least about 25% by weight docosahexaenoic acid.
  • the present invention is directed to a microbial oil comprising a triacylglycerol fraction of at least about 10% by weight, wherein at least about 12% by weight of the fatty acids in the triacylglycerol fraction is eicosapentaenoic acid, wherein at least about 25% by weight of the fatty acids in the triacylglycerol fraction is docosahexaenoic acid, and wherein less than about 5% by weight of the fatty acids in the triacylglycerol fraction is arachidonic acid.
  • the present invention is directed to a food product, cosmetic, or pharmaceutical composition for a non-human animal or human, comprising any of the microbial oils of the invention.
  • the food product is an infant formula.
  • the infant formula is suitable for premature infants.
  • the food product is a milk, a beverage, a therapeutic drink, a nutritional drink, or a combination thereof.
  • the food product is an additive for the non- human animal or human food.
  • the food product is a nutritional supplement.
  • the food product is an animal feed.
  • the animal feed is an aquaculture feed.
  • the animal feed is a domestic animal feed, a zoological animal feed, a work animal feed, a livestock feed, or a combination thereof.
  • the present invention is directed to a method for producing a microbial oil comprising omega-3 fatty acids, the method comprising: growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce an oil comprising omega-3 fatty acids. In some embodiments, the method further comprises extracting the oil.
  • the present invention is directed to a method for producing a microbial oil comprising omega-3 fatty acids, the method comprising extracting an oil comprising omega-3 fatty acids from any of the biomasses of the invention.
  • the microbial oil is extracted using an organic solvent extraction process, for example hexane extraction.
  • the microbial oil is extracted using a solventless extraction process.
  • the present invention is directed to a microbial oil produced by a method of the invention.
  • the present invention is directed to a method for producing a biomass of the invention, comprising: growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce a biomass.
  • the present invention is directed to a biomass produced by a method of the invention.
  • the present invention is directed to a method for producing a mutant strain of the invention, comprising: mutagenizing any of the microorganisms of the invention, and isolating the mutant strain.
  • the present invention is directed to use of any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, for the manufacture of a medicament for treatment of inflammation or a condition related thereto.
  • the present invention is directed to use of any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, for treatment of inflammation or a condition related thereto.
  • the present invention is directed to any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, for use in treatment of inflammation or a condition related thereto.
  • the present invention is directed to a method for treating inflammation or a condition related thereto in a subject in need thereof, comprising administering to the subject any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, and a pharmaceutically acceptable carrier.
  • the present invention is directed to isolated microorganisms, as well as strains and mutants thereof, as well as biomasses, microbial oils, compositions, and cultures thereof.
  • the present invention is directed to methods of producing microbial oils, biomasses, and mutants from the microorganisms of the invention, and methods of using the microorganisms, biomasses, and microbial oils.
  • the microorganisms described herein are highly productive and produce unique fatty acid profiles, characterized in part by high levels of omega- 3 fatty acids, in particular high levels of EPA.
  • the invention is directed to isolated microorganisms and strains derived therefrom.
  • a strain that is "derived" from an isolated microorganism of the invention can be a natural or artificial derivative such as, for example, a mutant, variant, or recombinant strain.
  • isolated does not necessarily reflect the extent to which an isolate has been purified, but indicates isolation or separation from a native form or native environment.
  • An isolate can include, but is not limited to, an isolated microorganism, an isolated biomass, an isolated culture, an isolated microbial oil, and an isolated sequence (such as an isolated polynucleotide sequence disclosed herein).
  • microorganism as used herein includes, but is not limited to, the terms “microalgae,” “thraustochytrid,” and taxonomic classifications associated with any of the deposited microorganisms described herein.
  • Thraustochytriales as used in reference to any of the microorganisms of the invention, including the deposited microorganisms described herein, are based on present taxonomic classifications including available phylogenetic information and are not intended to be limiting in the event that the taxonomic classifications are revised after the filing date of the present application.
  • the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA-10212.
  • the isolated microorganism associated with ATCC Accession No. PTA-10212 is also known herein as Thraustochytrium sp. ATCC PTA-10212.
  • the isolated microorganism associated with ATCC Accession No. PTA-10212 was deposited under the Budapest Treaty on July 14, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 20110-2209.
  • the invention is directed to an isolated strain deposited under ATCC Accession No. PTA-10212.
  • the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10212 or a strain derived therefrom.
  • the characteristics of the species deposited under ATCC Accession No. PTA-10212 can include its growth and phenotypic properties (examples of phenotypic properties include morphological and reproductive properties), its physical and chemical properties (such as dry weights and lipid profiles), its gene sequences, and combinations thereof, in which the characteristics distinguish the species over previously identified species.
  • the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No.
  • PTA-10212 wherein the characteristics include an 18s rRNA comprising the polynucleotide sequence of SEQ ID NOT or a polynucleotide sequence having at least 94%, 95%, 96%, 97%, 98%, or 99% identity to SEQ ID NOT , the morphological and reproductive properties of the species deposited under ATCC Accession No. PTA- 10212, and the fatty acid profiles of the species deposited under ATCC Accession No. PTA-10212.
  • isolated microorganisms of the invention have phenotypic properties substantially identical to those of the microorganism deposited under ATCC Accession No. PTA-10212.
  • isolated microorganisms of the invention have growth properties substantially identical to those of the microorganism deposited under ATCC Accession No. PTA-10212.
  • the invention is directed to an isolated microorganism comprising an 18s rRNA comprising the polynucleotide sequence of SEQ ID NO: l or a polynucleotide sequence having at least 94%, 95%, 96%, 97%, 98%, or 99% identity to SEQ ID NO: l .
  • the invention is directed to an isolated microorganism comprising an 18s rRNA polynucleotide sequence that has at least 94% identity to the 18s rRNA polynucleotide sequence of the microorganism deposited under ATCC Accession No. PTA- 10212.
  • the invention is directed to a mutant strain of the microorganism deposited under ATCC Accession No. PTA- 10212.
  • the mutant strain is a strain deposited under ATCC Accession No. PTA- 10213, PTA-10214, or PTA-10215.
  • the microorganisms associated with ATCC Accession Nos. PTA-10213, PTA-10214, and PTA-10215 were deposited under the Budapest Treaty on July 14, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 201 10-2209.
  • the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA-10208.
  • the isolated microorganism associated with ATCC Accession No. PTA-10208 is also known herein as Schizochytrium sp. ATCC PTA-10208.
  • the microorganism associated with ATCC Accession No. PTA-10208 was deposited under the Budapest Treaty on July 14, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 20110-2209.
  • the invention is directed to an isolated strain deposited under ATCC Accession No. PTA-10208.
  • the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA-10208, wherein the total fatty acids produced by the microorganism comprises more than about 10%, more than about 11%, more than about 12%, more than about 13%, more than about 14%, more than about 15%, more than about 16%, more than about 17%, more than about 18%, more than about 19%, or more than about 20% by weight EPA.
  • the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No.
  • the total fatty acids produced by the microorganism comprises about 10% to about 55%, about 10% to about 50%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, about 20% to about 55%, about 20% to about 50%, about 20% to about 45%, about 20% to about 40%, about 20% to about 35%, or about 20% to about 30% o by weight EPA.
  • the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10%) by weight eicosapentaenoic acid.
  • the characteristics of the microorganism deposited under ATCC Accession No. PTA- 10208 include its growth and phenotypic properties (examples of phenotypic properties include morphological and reproductive properties), its physical and chemical properties (such as dry weights and lipid profiles), its gene sequences, and combinations thereof, in which the characteristics distinguish the species over previously identified species.
  • the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10212, wherein the characteristics include an 18s rRNA comprising the polynucleotide sequence of SEQ ID NO:2, the morphological and reproductive properties of the species deposited under ATCC Accession No. PTA- 10208, and the fatty acid profiles of the species deposited under ATCC Accession No. PTA- 10208.
  • isolated microorganisms of the invention have physical and chemical properties substantially identical to those of the microorganism deposited under ATCC Accession No. PTA-10208.
  • the invention is directed to a mutant strain of the microorganism deposited under ATCC Accession No. PTA-10208.
  • the mutant strain is a strain deposited under ATCC Accession No. PTA- 10209, PTA-10210, or PTA-1021 1.
  • the microorganisms associated with ATCC Accession Nos. PTA-10209, PTA-10210, and PTA-1021 1 were deposited under the Budapest Treaty on September 25, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 20110-2209.
  • the invention is directed to an isolated microorganism of the invention that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight.
  • the invention is directed to an isolated microorganism that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is about 12% to about 55%, about 12 % to about 50%, about 12% to about 45%, about 12% to about 40%, about 12% to about 35%, about 12% to about 30%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, or about 20% o to about 30% by weight.
  • the invention is directed to a mutant, variant, or recombinant of an isolated microorganism of the invention that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is at least about 10%, at least about 1 1%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight.
  • the invention is directed to a mutant, variant, or recombinant of an isolated microorganism of the invention that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is about 12% to about 55%, about 12% to about 50%, about 12% to about 45%, about 12% to about 40%, about 12% to about 35%, about 12% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, about 20% to about 55%, about 20% to about 50%, about 20% to about 45%, about 20% to about 40%, about 20% to about 35%, or about 20% to about 30% by weight.
  • Mutant strains can be produced by well-known procedures. Common procedures include irradiation, treatment at high temperatures, and treatment with a mutagen. Variant strains can be other naturally occurring isolates and/or sub-isolates of the species described herein. Recombinant strains can be produced by any well-known methods in molecular biology for the expression of exogenous genes or alteration of endogenous gene function or expression. In some embodiments, the mutant, variant, or recombinant strain produces a higher amount of omega-3 fatty acids, particularly EPA, than the wild-type strain. In some embodiments, the mutant, variant, or recombinant strain produces a lower amount of one or more fatty acids, such as lower amounts of DHA, ARA, DPA n-6, or combinations thereof.
  • the mutant, variant, or recombinant strain produces a larger dry cell weight per liter of culture than the wild-type strain.
  • Such mutant, variant, or recombinant strains are examples of strains derived from an isolated microorganism of the invention.
  • an isolated microorganism of the invention, including mutants, variants, and recombinants thereof, comprises a fatty acid profile in one or more fractions isolated from the microorganism.
  • the one or more fractions isolated from the microorganism include the total fatty acid fraction, the sterol esters fraction, the triacylglycerol fraction, the free fatty acid fraction, the sterol fraction, the diacylglycerol fraction, the polar fraction (including the phospholipid fraction), and combinations thereof.
  • the fatty acid profile for a specific fraction can include any of the fatty acid profiles associated with the specific fraction as disclosed herein.
  • the invention is directed to a method of producing a mutant comprising mutagenizing any of the microorganisms of the invention and isolating the mutant strain.
  • the invention is directed to a culture comprising one or more isolated microorganisms of the invention.
  • Various fermentation parameters for inoculating, growing, and recovering microflora such as microalgae and thraustochytrids, are known in the art. See, e.g., U.S. Patent No. 5,130,242, incorporated by reference herein in its entirety.
  • Liquid or solid media can contain natural or artificial sea water.
  • Carbon sources for heterotrophic growth include, but are not limited to, glucose, fructose, xylose, saccharose, maltose, soluble starch, molasses, fucose, glucosamine, dextran, fats, oils, glycerol, sodium acetate, and mannitol.
  • Nitrogen sources include, but are not limited to, peptone, yeast extract, polypeptone, malt extract, meat extract, casamino acid, corn steep liquor, organic nitrogen sources, sodium glutamate, urea, inorganic nitrogen sources, ammonium acetate, ammonium sulfate, ammonium chloride, and ammonium nitrate.
  • KC1 g/L 1.0 0-5, 0.25-3, or 0.5-2
  • T 154 yeast extract g/L 6.0 0-20, 0.1-10, or 1-7
  • Citric acid mg/L 3.5 0.1-5000, 10-3000, or 3-2500
  • FeS0 4 -7H 2 0 mg/L 10.30 0.1-100, 1-50, or 5-25
  • MnCl 2 -4H 2 0 mg/L 3.10 0.1-100, 1-50, or 2-25
  • ZnS0 4 -7H 2 0 mg/L 3.10 0.01-100, 1-50, or 2-25
  • NiS0 4 -6H 2 0 mg/L 2.07 0.1-100, 0.5-50, or 1-25
  • Typical cultivation conditions would include the following: pH about 6.5 - about 9.5, about 6.5 - about 8.0, or about 6.8 - about 7.8;
  • dissolved oxygen about 0.1 - about 100% saturation, about 5 - about 50% saturation, or about 10 - about 30% saturation; and/or glycerol controlled @: about 5 - about 50 g/L, about 10 - about 40 g/L, or about
  • PTA-10212 or a mutant, variant, or recombinant thereof, grows heterotrophically on glycerol as the carbon source but does not grow on glucose as the carbon source.
  • KC1 g/L 1.0 0-5, 0.25-3, or 0.5-2
  • T 154 yeast extract g/L 1.0 0-20, 0.1-10, or 0.5-5
  • FeS0 4 -7H 2 0 mg/L 10.30 0.1-100, 1-50, or 5-25
  • MnCl 2 -4H 2 0 mg/L 3.10 0.1-100, 1-50, or 2-25
  • NiS0 4 '6H 2 0 mg/L 2.07 0.1- 100, 0.5-50, or 1-25
  • Typical cultivation conditions would include the following: pH about 6.5 - about 8.5, about 6.5 - about 8.0, or about 7.0 - about 8.0;
  • dissolved oxygen about 2 - about 100% saturation, about 5 - about 50% saturation, or about 7 - about 20% saturation; and/or glucose controlled about 5 - about 50 g/L, about 10 - about 40 g/L, or about 20 - about 35 g/L.
  • the culture medium comprises at least about 0.1%, at least about 0.5%, at least about 1%, at least about 1.5%, at least about 2%, at least about 5%, at least about 7%, at least about 10%, at least about 20%, at least about 30%, at least about 40%, at least about 50%, at least about 60%, at least about 70%, at least about 80%, or at least about 90% dissolved oxygen, as a percentage of saturation level.
  • the culture medium comprises about 0.1 % to about 2%, about 0.1 % to about 5%, about 0.1 % to about 10%, about 0.1% to about 20%, about 0.1 % to about 30%, about 0.1 % to about 50%, about 0.1% to about 100%, about 5% to about 10%, about 5% to about 20%, about 5% to about 30%, about 5% to about 50%, about 5% to about 100%, about 7% to about 10%, about 7% to about 20%, about 7% to about 30%, about 7% to about 50%, about 7% to about 100%, about 10% to about 20%, about 10% to about 30%, about 10% to about 50%, about 10% to about 100%, about 20% to about 30%, about 20% to about 50%, or about 20% to about 100% dissolved oxygen, as a percentage of saturation level.
  • the invention is directed to an isolated biomass of a microorganism of the invention.
  • An isolated biomass of the invention is a harvested cellular biomass obtained by any conventional method for the isolation of a biomass, such as described in U.S. Patent No. 5, 130,242 and U.S. Appl. Publ. No. 2002/0001833, each of which are incorporated by reference herein in its entirety.
  • the dry cell weight of the biomass isolated from each liter of culture is at least about 10 g, at least about 15 g, at least about 20 g, at least about 25 g, at least about 30 g, at least about 50 g, at least about 60 g, at least about 70 g, at least about 80 g, at least about 100 g, at least about 120 g, at least about 140 g, at least about 160 g, at least about 180 g, or at least about 200 g after growing for about 6 days to about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions.
  • the dry cell weight of the biomass isolated from each liter of culture is at least about 10 g, at least about 15 g, at least about 20 g, at least about 25 g, at least about 30 g, at least about 50 g, at least about 60 g, at least about 70 g, at least about 80 g, at least about 100 g, at least about 120 g, at least about 140 g, at least about 160 g, at least about 180 g, or at least about 200 g after growing for about 6 days, about 7 days, or about 8 days at about 15°C, about 16°C, about 17°C, at about 1 8°C, at about 19°C, at about 20°C, at about 21 °C, at about 22°C, at about 23°C, at about 24°C, at about 25°C, at about 26°C, at about 27°C, at about 28°C, at about 29°C, or at about 30°C in a culture medium of about pH 6.5, about pH 7, about pH 7.5,
  • the dry cell weight of the biomass isolated from each liter of culture is about 10 g to about 200 g after growing for about 6 days to about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions.
  • the dry cell weight of the biomass isolated from each liter of culture is about 10 g to about 200 g, about 10 g to about 100 g, about 10 g to about 50 g, about 15 g to about 200 g, about 15 g to about 100 g, about 15 g to about 50 g, about 20 g to about 200 g, about 20 g to about 100 g, about 20 g to about 50 g, about 50 g to about 200 g, or about 50 g to about 100 g after growing for about 6 days, about 7 days, or about 8 days at about 15°C, about 16°C, about 17°C, at about 18°C, at about 19°C, at about 20°C, at about 21°C, at about 22°C, at about 23°C, at about 24°C, at about 25°C, at about 26°C, at about 27°C, at about 28°C, at about 29°C, or at about 30°C in a culture medium of about pH 6.5, about pH 7, about pH
  • the isolated culture has an omega- 3 fatty acid productivity of at least about 0.2 g/L/day, at least about 0.3 g/L/day, at least about 0.4 g/L/day, at least about 0.5 g/L/day, at least about 1 g/L/day, at least about 1.2 g/L/day, at least about 1.5 g/L/day, at least about 1.7 g/L/day, at least about 2 g/L/day, at least about 3 g/L/day, at least about 3.5 g/L/day, at least about 4 g/L/day, at least about 4.5 g/L/day, at least about 5 g/L/day, at least about 6 g/L/day, or at least about 8 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 8.5 or about pH 6.5 to about pH 9.5 comprising sources
  • the isolated culture has an omega-3 fatty acid productivity of about 0.2 g/L/day to about 20 g/L/day, about 0.4 g/L/day to about 20 g/L/day, about 0.4 g/L/day to about 2 g/L/day, about 1 g/L/day to about 2 g/L/day, about 1 g/L/day to about 20 g/L/day, about 2 g/L/day to about 15 g/L/day, about 2 g/L/day to about 10 g/L/day, about 3 g/L/day to about 10 g/L/day, about 4 g/L/day to about 9 g/L/day, about 4 g/L/day to about 8 g/L/day, about 4 g/L/day to about 7 g/L/day, or about 4 g/L/day to about 6 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°
  • the isolated culture comprises an EPA productivity of at least about 0.2 g/L/day, at least about 0.3 g/L/day, at least about 0.4 g/L/day, at least about 0.5 g/L/day, at least about 0.6 g/L/day, at least about 0.7 g/L/day, at least about 0.8 g/L/day, at least about 0.9 g/L/day, at least about 1 g/L/day, at least about 1.2 g/L/day, at least about 1.5 g/L/day, at least about 1.7 g/L/day, at least about 2 g/L/day, at least about 3 g/L/day, at least about 4 g/L/day, or at least about 5 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 8.5 or about pH 6.5 to about pH 9.5 comprising sources of carbon
  • the EPA productivity is about 0.2 g/L/day to about 5 g/L/day, about 0.2 g/L/day to about 4 g/L/day, about 0.2 g/L/day to about 3 g/L/day, about 0.2 g/L/day to about 2 g/L/day, about 0.2 g/L/day to about 1 g/L/day, about 0.2 g/L/day to about 0.8 g/L/day, about 0.2 g/L/day to about 0.7 g/L/day, about 1 g/L/day to about 5 g/L/day, about 1 g/L/day to about 4 g/L/day, about 1 g/L/day to about 3 g/L/day, or about 1 g/L/day to about 2 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH
  • any of the aforementioned EPA productivities are associated with any of the aforementioned omega- 3 fatty acid productivities.
  • the culture further comprises a DHA productivity of about 0 g/L/day to about 5 g/L/day, about 0 g/L/day to about 4 g/L/day, about 0 g/L/day to about 3 g/L/day, about 0 g/L/day to about 2 g/L/day, about 0 g/L/day to about 1 g/L/day, about 0.2 g/L/day to about 5 g/L/day, about 0.2 g/L/day to about 4 g/L/day, about 0.2 g/L/day to about 3 g/L/day, about 0.2 g/L/day to about 2 g/L/day, about 0.2 g/L/day to about 1 g/L/day, about 1 g/L/day to about 5 g/L/day.
  • the DHA productivity is less than about 5 g/L/day, less than about 4 g/L/day, less than about 3 g/L/day, less than about 2 g/L/day, less than about 1 g/L/day, less than about 0.5 g/L/day, less than about 0.2 g/L/day, or about 0 g/L/day.
  • the fermentation volume is at least about 2 liters, at least about 10 liters, at least about 50 liters, at least about 100 liters, at least about 200 liters, at least about 500 liters, at least about 1000 liters, at least about 10,000 liters, at least about 20,000 liters, at least about 50,000 liters, at least about 100,000 liters, at least about 150,000 liters, at least about 200,000 liters, or at least about 250,000 liters.
  • the fermentation volume is about 2 liters to about 300,000 liters, about 2 liters, about 10 liters, about 50 liters, about 100 liters, about 200 liters, about 500 liters, about 1000 liters, about 10,000 liters, about 20,000 liters, about 50,000 liters, about 100,000 liters, about 150,000 liters, about 200,000 liters, about 250,000 liters, or about 300,000 liters.
  • the invention is directed to an isolated biomass comprising a fatty acid profile of the invention.
  • at least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%, at least about 45%, at least about 50%, at least about 55%, at least about 60%, at least about 65%, at least about 70%), at least about 75%, or at least about 80% of the dry cell weight of the biomass are fatty acids.
  • greater than about 20%, greater than about 25%, greater than about 30%, greater than about 35%, greater than about 40%, greater than about 45%, greater than about 50%, greater than about 55%, or greater than about 60% of the dry cell weight of the biomass are fatty acids.
  • about 20% to about 55%, about 20% to about 60%, about 20% to about 70%, about 20% to about 80%, about 30% to about 55%, about 30% to about 70%, about 30% to about 80%, about 40% to about 60%, about 40% to about 70%, about 40% to about 80%, about 50% to about 60%, about 50% to about 70%, about 50% to about 80%, about 55% to about 70%, about 55% to about 80%, about 60% to about 70%, or about 60% to about 80% by weight of the dry cell weight of the biomass are fatty acids.
  • the biomass comprises more than about 10%, at least about 12%, at least about 15%, at least about 20%, at least about 25%, at least about 30%, about least about 35%, at least about 40%, or at least about 45% by weight of the fatty acids as EPA. In some embodiments, the biomass comprises about 10% to about 55%, about 12% to about 55%, about 15% to about 55%, about 20% to about 55%, about 20% to about 40%, or about 20% to about 30% by weight of the fatty acids as EPA.
  • the biomass comprises a triacylglycerol fraction, wherein at least about 12%, at least about 13%, at least about 14%), at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight of the triacylglycerol fraction is EPA.
  • the biomass comprises a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is from at least about 12% to about 55%, about 12% to about 50%, about 12% to about 45%, at least about 12% to about 40%, at least about 12% to about 35%, or at least about 12% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, about 20% to about 55%, about 20% to about 50%, about 20% to about 45%, at least about 20% to about 40%o, at least about 20% to about 35%, or about 20% to about 30% by weight.
  • the EPA content of the triacylglycerol fraction is from at least about 12% to about 55%, about 12% to about 50%, about 12% to about 45%, at least about 12% to about 40%, at least about 12% to about 35%, or at least about 12% to about 30%, about 15% to about 55%, about 15% to
  • At least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%, at least about 50%, or at least about 60% by weight of the dry cell weight of the biomass is DHA.
  • about 20% to about 60%, about 25%o to about 60%, about 25% to about 50%), about 25% to about 45%, about 30% to about 50%, or about 35% to about 50% by weight of the dry cell weight of the biomass is DHA.
  • the biomass comprises about 10% or less, about 9% or less, about 8% or less, about 7% or less, about 6% or less, about 5% or less, about 4% or less, about 3% or less, about 2% or less, or about 1% or less by weight of the fatty acids as DHA.
  • the biomass comprises about 1% to about 10%, about 1% to about 5%, about 2% to about 5%, about 3% to about 5%, or about 3% to about 10% by weight of the fatty acids as DHA. In some embodiments, the biomass is substantially free of DHA.
  • the biomass comprises about 0.1% to less than about 5%, about 0.1% to about 4%, about 0.1% to about 3%, about 0.1% to about 2%, about 0.2% to less than about 5%, about 0.2% to about 4%, about 0.2% to about 3%, about 0.2% to about 2%, about 0.3% to about 2%, about 0.1% to about 0.5%, about 0.2%> to about 0.5%, about 0.1% to about 0.4%, about 0.2% to about 0.4%, about 0.5% to about 2%, about 1% to about 2%, about 0.5%o to about 1.5%>, or about 1%> to about 1.5%> by weight of the fatty acids as ARA.
  • the biomass comprises less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1.5% or less, about 1% or less, about 0.5% or less, about 0.4% or less, about 0.3% or less, about 0.2% or less, or about 0.1% or less by weight of the fatty acids as ARA. In some embodiments, the biomass is substantially free of ARA.
  • the biomass comprises about 0.4% to about 2%, about 0.4% to about 3%, about 0.4% to about 4%, about 0.4% to about 5%, about 0.4% to less than about 5%, about 0.5% to about 1%, about 0.5% to about 2%, about 0.5% to about 3%, about 0.5% to about 4%, about 0.5% to about 5%, about 0.5% to less than about 5%, about 1% to about 2%, about 1% to about 3%, about 1% to about 4%, about 1% to about 5%, or about 1% to less than about 5% by weight of the fatty acids as DPA n-6.
  • the biomass comprises about 5% or less, less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.75% or less, about 0.6% or less, or about 0.5% or less by weight of the fatty acids as DPA n-6. In some embodiments, the biomass is substantially free of DPA n-6.
  • the biomass comprises fatty acids with about 5% or less, less than about 5%, about 4% or less, about 3% or less, or about 2% or less by weight of oleic acid (18: 1 n-9), linoleic acid (18:2 n-6), linolenic acid (18:3 n-3), eicosenoic acid (20: 1 n-9), erucic acid (22: 1 n-9), or combinations thereof.
  • an isolated biomass of the invention is associated with endogenous or native properties of the isolated biomass rather than exogenously introduced materials.
  • the isolated biomass does not contain polyvinylpyrrolidone or is not isolated from a culture containing polyvinylpyrrolidone.
  • the present invention is directed to a method of producing a biomass.
  • the method for producing a biomass of the invention comprises growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce a biomass.
  • the present invention is directed to a biomass produced by the method.
  • the invention is directed to a microbial oil comprising a fatty acid profile of the invention.
  • a microbial oil of the invention is a "crude oil” or a “refined oil” comprising a triacylglycerol fraction of at least about 35% by weight.
  • a “crude oil” is an oil that is extracted from the biomass of the microorganism without further processing.
  • a “refined oil” is an oil that is obtained by treating a crude oil with standard processing of refining, bleaching, and/or deodorizing. See, e.g., U.S. Patent No. 5,130,242, incorporated by reference herein in its entirety.
  • a microbial oil also includes a "final oil” as described herein, which is a refined oil that has been diluted with a vegetable oil.
  • a final oil is a refined oil that has been diluted with high oleic sunflower oil.
  • the term "microbial” as used herein includes, but is not limited to, the terms “microalgal,” “thraustochytrid,” and taxonomic classifications associated with any of the deposited microorganisms described herein.
  • Thraustochytriales as used in reference to any of the microbial oils of the deposited microorganisms described herein are based on present taxonomic classifications including available phylogenetic information and are not intended to be limiting in the event that the taxonomic classifications are revised after the filing date of the present application.
  • a fatty acid as described herein can be a fatty acid ester.
  • a fatty acid ester includes an ester of an omega-3 fatty acid, omega-6 fatty acid, and combinations thereof.
  • the fatty acid ester is a DHA ester, an EPA ester, or a combination thereof.
  • an oil or fraction thereof as described herein is esterified to produce an oil or fraction thereof comprising fatty acid esters.
  • esteer refers to the replacement of the hydrogen in the carboxylic acid group of the fatty acid molecule with another substituent. Typical esters are known to those in the art, a discussion of which is provided by Higuchi, T. and V.
  • esters include methyl, ethyl, propyl, butyl, pentyl, t-butyl, benzyl, nitrobenzyl, methoxybenzyl, benzhydryl, and trichloroethyl.
  • the ester is a carboxylic acid protective ester group, esters with aralkyl (e.g., benzyl, phenethyl), esters with lower alkenyl (e.g., allyl, 2- butenyl), esters with lower-alkoxy-lower-alkyl (e.g., methoxymethyl, 2-methoxyethyl, 2- ethoxyethyl), esters with lower- alkanoyloxy- lower- alkyl (e.g., acetoxymethyl, pivaloyloxymethyl, 1-pivaloyloxyethyl), esters with lower-alkoxycarbonyl-lower-alkyl (e.g., methoxycarbonylmethyl, isopropoxycarbonylmethyl), esters with carboxy-lower alkyl (e.g., carboxymethyl), esters with lower-alkoxycarbonyloxy-lower-alkyl (e.g., 1- (e
  • the added substituent is a linear or cyclic hydrocarbon group, e.g., a C1-C6 alkyl, C1-C6 cycloalkyl, C1-C6 alkenyl, or C1-C6 aryl ester.
  • the ester is an alkyl ester, e.g., a methyl ester, ethyl ester or propyl ester.
  • the ester substituent is added to the free fatty acid molecule when the fatty acid is in a purified or semi-purified state. Alternatively, the fatty acid ester is formed upon conversion of a triacylglycerol to an ester.
  • the present invention is directed to methods of producing microbial oils.
  • the method comprises growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce a microbial oil comprising omega-3 fatty acids.
  • the method further comprises extracting the microbial oil.
  • the method comprises extracting a microbial oil comprising omega-3 fatty acids from any of the biomasses of the invention or mixtures thereof.
  • the method comprises heterotrophically growing the isolated microorganism, wherein the culture comprises a carbon source as described herein.
  • the microbial oil can be extracted from a freshly harvested biomass or can be extracted from a previously harvested biomass that has been stored under conditions that prevent spoilage.
  • Known methods can be used to culture a microorganism of the invention, to isolate a biomass from the culture, to extract a microbial oil from the biomass, and to analyze the fatty acid profile of oils extracted from the biomass. See, e.g., U.S. Patent No. 5,130,242, incorporated by reference herein in its entirety.
  • the invention is directed to a microbial oil produced by any of the methods of the invention.
  • the microbial oil is extracted by an enzyme extraction method.
  • the microbial oil is extracted by a mechanical extraction method.
  • the mechanical extraction method comprises one or more of: (1) processing a pasteurized fermentation broth through a homogenizer to assist in cell lysis and release of oil from cells; (2) adding isopropyl alcohol to the fermentation broth following homogenization to break the oil and water emulsion; (3) centrifuging the mixture to recover the oil phase; and (4) drying under vacuum with addition of antioxidants.
  • the crude oil is purified.
  • purification of the crude oil comprises one or more of: (1) pumping the crude oil into a refining tank and heating the oil, followed by adding an acid solution with mixing; (2) adding a caustic solution to the oil after acid treatment; (3) reheating the crude oil and then centrifuging to separate the heavy phase from the refined oil; (4) removing the remaining polar compounds, trace metals, and oxidation products from the refined oil by using, for example, acid, TriSyl®, clay, and/or filtration; (5) chill filtering the bleached oil to further remove high melting point components from the oil to achieve the desired level of clarity; (6) heating the oil, after which the oil is then cooled and held for a period of time causing the high melting triglycerides and waxes to crystallize; (7) adding a filter aid to the chilled oil and then removing crystallized solids by filtration; (8) using a deodorizer after chill filtration, operated under high temperature and vacuum, to remove, for example, peroxides and any remaining low
  • the microbial oil comprises a sterol esters fraction of about
  • the microbial oil comprises a sterol esters fraction of about 0% to about 1.5%, about 0% to about 2%, about 0% to about 5%, about 1% to about 1.5%, about 0.2% to about 1.5%, about 0.2% to about 2%, or about 0.2%> to about 5% by weight.
  • the microbial oil comprises a sterol esters fraction of about 5% or less, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.5% or less, about 0.3% or less, about 0.2% 0 or less, about 0.5% or less, about 0.4% or less, about 0.3% or less, or about 0.2% or less by weight.
  • the microbial oil comprises a triacylglycerol fraction of at least about 35%, at least about 40%, at least about 45%, at least about 50%, at least about 55%, at least about 60%, at least about 65%, at least about 70%>, at least about 75%, at least about 80%, at least about 85%, or at least about 90% by weight.
  • the microbial oil comprises a triacylglycerol fraction of about 35% to about 98%, about 35% to about 90%, about 35% to about 80%, about 35% to about 70%, about 35% to about 70%, about 35% to about 65%, about 40% to about 70%, about 40% to about 65%, about 40% to about 55%, about 40% to about 50%, about 65% to about 95%, about 75% to about 95%, about 75% to about 98%, about 80% to about 95%, about 80% to about 98%, about 90% to about 96%, about 90% to about 97%, about 90% to about 98%, about 90%, about 95%, about 97%, or about 98% by weight.
  • the microbial oil comprises a diacylglycerol fraction of at least about 10%, at least about 1 1%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight.
  • the microbial oil comprises a diacylglycerol fraction of about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 15% to about 40%, about 15% to about 35%, or about 15% to about 30% by weight.
  • the microbial oil comprises a 1 ,2-diacylglycerol fraction of at least about 0.2%, at least about 0.3%, at least about 0.4%, at least about 0.5%, at least about 1%, at least about 5%, at least about 10%, at least about 11%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight.
  • a 1 ,2-diacylglycerol fraction of at least about 0.2%, at least about 0.3%, at least about 0.4%, at least about 0.5%, at least about 1%, at least about 5%, at least about 10%, at least about 11%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight.
  • the microbial oil comprises a diacylglycerol fraction of about 0.2%> to about 45%, about 0.2% to about 30%, about 0.2% to about 20%, about 0.2% to about 10%, about 0.2% to about 5%, about 0.2% to about 1%, about 0.2% to about 0.8%, about 0.4% to about 45%, about 0.4% to about 30%, about 0.4% to about 20%, about 0.4% to about 10%, about 0.4% to about 5%, about 0.4% to about 1%, about 0.4% to about 0.8%, about 0.5% to about 1%, about 0.5% to about 0.8%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 15% to about 40%, about 15% to about 35%, about 15%) to about 30%), or about 15% to about 25% by weight.
  • the microbial oil comprises a 1,3-diacylglycerol fraction of at least about 0.1%, at least about 0.2%, at least about 0.5%, at least about 1%, at least about 2%, at least about 2.5 %, or at least about 3% by weight. In some embodiments, the microbial oil comprises a sterol fraction of at least about 0.3%, at least about 0.4%, at least about 0.5%, at least about 1%, at least about 1.5%, at least about 2%>, or at least about 5% by weight.
  • the microbial oil comprises a sterol fraction of about 0.3% to about 5%, about 0.3% to about 2%, about 0.3% to about 1.5%, about 0.5% to about 1.5%, about 1% to about 1.5%, about 0.5% to about 2%, about 0.5% to about 5%, about 1% to about 2%, or about 1% to about 5% by weight. In some embodiments, the microbial oil comprises a sterol fraction of about 5% or less, about 4% or less, about 3% or less, about 2% or less, about 1.5% or less, or about 1% or less by weight.
  • the microbial oil comprises a phospholipid fraction of at least about 2%, at least about 5%, or at least about 8% by weight. In some embodiments, the microbial oil comprises a phospholipid fraction of about 2% to about 25%, about 2% to about 20%, about 2% to about 15%, about 2% to about 10%, about 5% to about 25%, about 5% to about 20%, about 5% to about 20%, about 5% to about 10%, or about 7% to about 9% by weight. In some embodiments, the microbial oil comprises a phospholipid fraction of less than about 20%, less than about 15%, less than about 10%, less than about 9%, or less than about 8% by weight. In some embodiments, the microbial oil is substantially free of phospholipids.
  • the microbial oil comprises unsaponifiables of less than about 2%, less than about 1.5%, less than about 1%, or less than about 0.5% by weight of the oil.
  • the lipid classes present in the microbial oil such as a triacylglycerol fraction, can be separated by flash chromatography and analyzed by thin layer chromatography (TLC), or separated and analyzed by other methods known in the art.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the free fatty acid fraction, the sterol fraction, the diacylglycerol fraction, and combinations thereof comprises at least about 5%, at least about 10%, more than about 10%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, at least about 20%, at least about 25%, at least about 30%, about least about 35%, at least about 40%, or at least about 45%o by weight EPA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the free fatty acid fraction, the sterol fraction, the diacylglycerol fraction, and combinations thereof comprises about 5% to about 55%, about 5% to about 50%, about 5% to about 45%, about 5% to about 40%, about 5% to about 35%, about 5% to about 30%, about 10% to about 55%, about 10% to about 50%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, at least about 12% to about 55%, at least about 12% to about 50%, at least about 12% to about 45%, at least about 12% to about 40%, at least about 12% to about 35%, or at least about 12% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%), about 15% to about 40%, about 15% to about 35%, about 15% to about 30%), about 15% to about 25%, about 15% to about 20%, about 20% to
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises at least about 5%, at least about 10%, at least about 15%, at least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%o, at least about 50% 0 , or at least about 60% by weight DHA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 5%> to about 60%, about 5% to about 55%, about 5% to about 50%, about 5% to about 40%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 20% to about 60%, about 25% to about 60%, about 25% to about 50%, about 25% to about 45%, about 30% to about 50%, about 35% to about 50%, or about 30% to about 40%) by weight DHA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 10% or less, about 9% or less, about 8% or less, about 7% or less, about 6% or less, about 5% or less, about 4% or less, about 3%> or less, about 2%> or less, or about ⁇ % or less by weight DHA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 1 % to about 10%, about 1% to about 5%, about 2% to about 5%, about 3% to about 5%>, or about 3% to about 10% by weight of the fatty acids as DHA.
  • the microbial oil and/Or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, is substantially free of DHA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 0.1% to about 5%, about 0.1% to less than about 5%, about 0.1% to about 4%, about 0.1% to about 3%, about 0.1% to about 2%, about 0.2%) to about 5%, about 0.2% to less than about 5%, about 0.2% to about 4%, about 0.2% to about 3%, about 0.2% to about 2%, about 0.3% to about 2%, about 0.1% to about 0.5%, about 0.2% to about 0.5%, about 0.1 % to about 0.4%, about 0.2% to about 0.4%, about 0.5% to about 2%, about 1 % to about 2%, about 0.5% to about 1.5%, or about 1% to about 1.5% by weight A A.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 5% or less, less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1.5% or less, about 1% or less, about 0.5% or less, about 0.4% or less, about 0.3%o or less, about 0.2% or less, or about 0.1% or less by weight ARA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, is substantially free of ARA.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 0.4% to about 2%, about 0.4% to about 3%, about 0.4% to about 4%, about 0.4%) to about 5%, about 0.4% to less than about 5%, about 0.5% to about 1%, about 0.5% to about 2%, about 0.5% to about 3%, about 0.5% to about 4%, about 0.5% to about 5%, about 0.5% to less than about 5%, about 1 % to about 2%, about 1 % to about 3%, about 1% to about 4%, about 1% to about 5%, or about 1% to less than about 5% by weight DPA n-6.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises about 5%, less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.75% or less, about 0.6% or less, or about 0.5%) or less by weight DPA n-6.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, is substantially free of DPA n-6.
  • the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof comprises fatty acids with about 5% or less, less than about 5%, about 4% or less, about 3% or less, or about 2% or less by weight of oleic acid (18: 1 n-9), linoleic acid (18:2 n-6), linolenic acid (18:3 n-3), eicosenoic acid (20: 1 n-9), erucic acid (22: 1 n-9), stearidonic acid (18:4 n-3), or combinations thereof.
  • the triacylglycerol molecule contains 3 central carbon atoms (C(-S7i-l)H 2 Rl-(s «-
  • the microbial oil comprises a triacylglycerol fraction in which at least about 2%, at least about 3%, at least about 5%, at least about 10%, at least about 15%, at least about 20%>, at least about 30%>, at least about 35%», or at least about 40%> of the triacylglycerols in the triacylglycerol fraction contain DHA at two positions in the triacylglycerol (di-substituted DHA) selected from any two of the sn-l, sn-2, and sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph.
  • the microbial oil comprises a triacylglycerol fraction in which about 2% to about 55%, about 2% to about 50%, about 2% to about 45%, about 2% to about 40%, about 2% to about 35%, about 2% to about 30%, about 2% to about 25%, about 5% to about 55%, about 5% to about 50%, about 5% to about 45%, about 5% to about 40%, about 5%) to about 35%, about 5% to about 30%, about 5% to about 25%, about 10% to about 55%o, about 10% to about 50%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 10% to about 25%, about 10% to about 20%), about 20% to about 40%, about 20% o to about 35%, or about 20% to about 25%o of the triacylglycerols in the triacylglycerol fraction contain EPA at two positions in the triacylglycerol selected from any two of the sn-l, sn-2, or
  • the microbial oil comprises a triacylglycerol fraction in which at least about 0.5%, at least about 1%, at least about 1.5%, or at least about 2% of the triacylglycerols in the triacylglycerol fraction contain DHA at all of the sn-l, sn-2, and sn-3 positions (tri- substituted DHA), based on the relative area percent of peaks on an HPLC chromatograph.
  • the microbial oil comprises a triacylglycerol fraction in which about 0.5% to about 5%, about 0.5% to about 3%, about 0.5% to about 2.5%, about 0.5%o to about 2%, about 1 % to about 5%, about 1 % to about 3%, or about 1 % to about 2%o of the triacylglycerols in the triacylglycerol fraction contain DHA at all of the sn-l, sn-2, and sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph.
  • the microbial oil comprises a triacylglycerol fraction in which at least about 10%, at least about 15%, at least about 20%, at least about 25%, at least about 30%, at least about 35%o, at least about 40%, at least about 45%, at least about 50%>, at least about 55%, or at least about 60% of the triacylglycerols in the triacylglycerol fraction contain DHA at one position in the triacylglycerol selected from any one of the sn-l, sn-2, or sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph.
  • the microbial oil comprises a triacylglycerol fraction in which about 10% to about 80%, about 10% to about 70%, about 10% to about 60%, about 15% to about 80%, about 15% to about 75%>, about 15% to about 70%, about 15% to about 65%, about 15% to about 60%, about 35% to about 80%, about 35% to about 75%, about 35% to about 65%, about 35% to about 60%o, about 40% to about 80%, about 40% to about 75%, about 40% to about 70%, about 40% to about 65%, about 40% o to about 60%, or about 40% to about 55% of the triacylglycerols in the triacylglycerol fraction contain DHA at one position in the triacylglycerol selected from any one of the sn-l, sn-2, and sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph.
  • the invention is directed to compositions comprising a microorganism of the invention, an isolated biomass of the invention, a microbial oil of the invention, or combinations thereof.
  • a microorganism, biomass, or microbial oil of the invention can be further chemically or physically modified or processed based on the requirements of the composition by any known technique.
  • Microorganism cells or biomasses can be dried prior to use in a composition by methods including, but not limited to, freeze drying, air drying, spray drying, tunnel drying, vacuum drying (lyophilization), and a similar process.
  • a harvested and washed biomass can be used directly in a composition without drying. See, e.g., U.S. Patent Nos. 5,130,242 and 6,812,009, each of which is incorporated by reference herein in its entirety.
  • Microbial oils of the invention can be used as starting material to more efficiently produce a product enriched in a fatty acid such as EPA.
  • a fatty acid such as EPA
  • the microbial oils of the invention can be subjected to various purification techniques known in the art, such as distillation or urea adduction, to produce a higher potency product with higher concentrations of EPA or another fatty acid.
  • the microbial oils of the invention can also be used in chemical reactions to produce compounds derived from fatty acids in the oils, such as esters and salts of EPA or another fatty acid.
  • a composition of the invention can include one or more excipients.
  • excipient refers to a component, or mixture of components, that is used in a composition of the present invention to give desirable characteristics to the composition, including foods as well as pharmaceutical, cosmetic, and industrial compositions.
  • An excipient of the present invention can be described as a "pharmaceutically acceptable" excipient when added to a pharmaceutical composition, meaning that the excipient is a compound, material, composition, salt, and/or dosage form which is, within the scope of sound medical judgment, suitable for contact with tissues of human beings and non- human animals without excessive toxicity, irritation, allergic response, or other problematic complications over the desired duration of contact commensurate with a reasonable benefit/risk ratio.
  • the term "pharmaceutically acceptable” means approved by a regulatory agency of the Federal or a state government or listed in the U.S. Pharmacopeia or other generally recognized international pharmacopeia for use in animals, and more particularly in humans.
  • Various excipients can be used.
  • the excipient can be, but is not limited to, an alkaline agent, a stabilizer, an antioxidant, an adhesion agent, a separating agent, a coating agent, an exterior phase component, a controlled-release component, a solvent, a surfactant, a humectant, a buffering agent, a filler, an emollient, or combinations thereof.
  • Excipients m addition to those discussed herein can include excipients listed in, though not limited to, Remington: The Science and Practice of Pharmacy, 21 st ed. (2005). Inclusion of an excipient in a particular classification herein (e.g., "solvent") is intended to illustrate rather than limit the role of the excipient. A particular excipient can fall within multiple classifications.
  • compositions of the invention include, but are not limited to, food products, pharmaceutical compositions, cosmetics, and industrial compositions.
  • the composition is a food product.
  • a food product is any food for non-human animal or human consumption, and includes both solid and liquid compositions.
  • a food product can be an additive to animal or human foods.
  • Foods include, but are not limited to, common foods; liquid products, including milks, beverages, therapeutic drinks, and nutritional drinks; functional foods; supplements; nutraceiiticals; infant formulas, including formulas for pre-mature infants; foods for pregnant or nursing women; foods for adults; geriatric foods; and animal foods.
  • a microorganism, biomass, or microbial oil of the invention can be used directly as or included as an additive within one or more of: an oil, shortening, spread, other fatty ingredient, beverage, sauce, dairy-based or soy-based food (such as milk, yogurt, cheese and ice-cream), a baked good, a nutritional product, e.g., as a nutritional supplement (in capsule or tablet form), a vitamin supplement, a diet supplement, a powdered drink, and a finished or semi-finished powdered food product.
  • the nutritional supplement is in the form of a vegetarian capsule that is not formed from and does not contain any components from an animal source.
  • a partial list of food compositions that can include a microbial oil of the invention includes, but is not limited to, soya based products (milks, ice creams, yogurts, drinks, creams, spreads, whiteners); soups and soup mixes; doughs, batters, and baked food items including, for example, fine bakery wares, breakfast cereals, cakes, cheesecakes, pies, cupcakes, cookies, bars, breads, rolls, biscuits, muffins, pastries, scones, croutons, crackers, sweet goods, snack cakes, pies, granola/snack bars, and toaster pastries; candy; hard confectionery; chocolate and other confectionery; chewing gum; liquid food products, for example milks, energy drinks, infant formula, carbonated drinks, teas, liquid meals, fruit juices, fruit-based drinks, vegetable-based drinks; multivitamin syrups, meal replacers, medicinal foods, and syrups; powdered beverage mixes; pasta; processed fish products; processed meat products; processed poultry products; gravies
  • a microbial oil of the invention can be used to supplement infant formula.
  • Infant formula can be supplemented with a microbial oil of the invention alone or in combination with a physically refined oil derived from an arachidonic acid (ARA)-producing microorganism.
  • ARA arachidonic acid
  • An ARA-producing microorganism for example, is Mortierella alpina or Mortierella sect, schmuckeri.
  • infant formulas can be supplemented with a microbial oil of the invention in combination with an oil rich in ARA, including ARASCO® (Martek Biosciences, Columbia, MD).
  • the composition is an animal feed.
  • An "animal” includes non-human organisms belonging to the kingdom Animalia, and includes, without limitation, aquatic animals and terrestrial animals.
  • the term "animal feed” or "animal food” refers to any food intended for non-human animals, whether for fish; commercial fish; ornamental fish; fish larvae; bivalves; mollusks; crustaceans; shellfish; shrimp; larval shrimp; artemia; rotifers; brine shrimp; filter feeders; amphibians; reptiles; mammals; domestic animals; farm animals; zoo animals; sport animals; breeding stock; racing animals; show animals; heirloom animals; rare or endangered animals; companion animals; pet animals such as dogs, cats, guinea pigs, rabbits, rats, mice, or horses; primates such as monkeys (e.g., cebus, rhesus, African green, patas, cynomolgus, and cercopithecus), apes, orangutans, bab
  • the composition is a feed or feed supplement for any animal whose meat or products are consumed by humans, such as any animal from which meat, eggs, or milk is derived for human consumption.
  • nutrients such as LC-PUFAs can be incorporated into the flesh, milk, eggs or other products of such animals to increase their content of these nutrients.
  • the composition is a spray-dried material that can be crumbled to form particles of an appropriate size for consumption by zooplankton, artemia, rotifers, and filter feeders.
  • the zooplankton, artemia, or rotifers fed by the composition are in turn fed to fish larvae, fish, shellfish, bivalves, or crustaceans.
  • the composition is a pharmaceutical composition.
  • suitable pharmaceutical compositions include, but are not limited to, an anti-inflammatory composition, a drug for treatment of coronary heart disease, a drug for treatment of arteriosclerosis, a chemotherapeutic agent, an active excipient, an osteoporosis drug, an anti-depressant, an anti-convulsant, an anti-Helicobacter pylori drug, a drug for treatment of neurodegenerative disease, a drug for treatment of degenerative liver disease, an antibiotic, a cholesterol lowering composition, and a triacylglycerol lowering composition.
  • the composition is a medical food.
  • a medical food includes a food that is in a composition to be consumed or administered externally under the supervision of a physician and that is intended for the specific dietary management of a condition, for which distinctive nutritional requirements, based on recognized scientific principles, are established by medical evaluation.
  • the microbial oil can be formulated in a dosage form.
  • Dosage forms can include, but are not limited to, tablets, capsules, cachets, pellets, pills, powders and granules, and parenteral dosage forms, which include, but are not limited to, solutions, suspensions, emulsions, and dry powders comprising an effective amount of the microbial oil. It is also known in the art that such formulations can also contain pharmaceutically acceptable diluents, fillers, disintegrants, binders, lubricants, surfactants, hydrophobic vehicles, water soluble vehicles, emulsifiers, buffers, humectants, moisturizers, solubilizers, preservatives and the like.
  • Administration forms can include, but are not limited to, tablets, dragees, capsules, caplets, and pills, which contain the microbial oil and one or more suitable pharmaceutically acceptable carriers.
  • the microbial oil can be combined with pharmaceutically acceptable carriers well known in the art.
  • Such carriers enable the microbial oils of the invention to be formulated as tablets, pills, dragees, capsules, liquids, gels, syrups, slurries, suspensions and the like, for oral ingestion by a subject to be treated.
  • the dosage form is a tablet, pill or caplet.
  • Pharmaceutical preparations for oral use can be obtained by adding a solid excipient, optionally grinding the resulting mixture, and processing the mixture of granules, after adding suitable auxiliaries, if desired, to obtain tablets or dragee cores.
  • Suitable excipients include, but are not limited to, fillers such as sugars, including, but not limited to, lactose, sucrose, mannitol, and sorbitol; cellulose preparations such as, but not limited to, maize starch, wheat starch, rice starch, potato starch, gelatin, gum tragacanth, methyl cellulose, hydroxypropylmethyl cellulose, sodium carboxymethyl cellulose, and polyvinylpyrrolidone (PVP).
  • disintegrating agents can be added, such as, but not limited to, the cross-linked polyvinylpyrrolidone, agar, or alginic acid or a salt thereof such as sodium alginate.
  • compositions that can be used orally include, but are not limited to, push- fit capsules made of gelatin, as well as soft, sealed capsules made of gelatin and a plasticizer, such as glycerol or sorbitol.
  • the dosage form is a vegetarian dosage form, in which the dosage form is not formed from and does not contain any components from an animal source. In some embodiments, the vegetarian dosage form is a vegetarian capsule.
  • the composition is a cosmetic.
  • Cosmetics include, but are not limited to, emulsions, creams, lotions, masks, soaps, shampoos, washes, facial creams, conditioners, make-ups, bath agents, and dispersion liquids.
  • Cosmetic agents can be medicinal or non-medicinal.
  • the composition is an industrial composition.
  • the composition is a starting material for one or more manufactures.
  • a manufacture includes, but is not limited to, a polymer; a photographic photosensitive material; a detergent; an industrial oil; or an industrial detergent.
  • U.S. Patent No. 7,259,006 describes use of DHA-containing fat and oil for production of behenic acid and production of photographic sensitive materials using behenic acid.
  • the compositions can be used in the treatment of a condition in humans or non-human animals. In some embodiments, the compositions can be used for nutrition in humans or non-human animals.
  • the terms “treat” and “treatment” refer to both therapeutic treatment and prophylactic or preventative measures, wherein the object is to prevent or slow down (lessen) an undesired physiological condition, disease, or disorder, or to obtain beneficial or desired clinical results.
  • beneficial or desired clinical results include, but are not limited to, alleviation or elimination of the symptoms or signs associated with a condition, disease, or disorder; diminishment of the extent of a condition, disease, or disorder; stabilization of a condition, disease, or disorder, (i.e., where the condition, disease, or disorder is not worsening); delay in onset or progression of the condition, disease, or disorder; amelioration of the condition, disease, or disorder; remission (whether partial or total and whether detectable or undetectable) of the condition, disease, or disorder; or enhancement or improvement of a condition, disease, or disorder.
  • Treatment includes eliciting a clinically significant response without excessive side effects. Treatment also includes prolonging survival as compared to expected survival if not receiving treatment.
  • the composition is used to treat a condition, disease, or disorder such as acne, acute inflammation, age related maculopathy, allergy, Alzheimer's, arthritis, asthma, atherosclerosis, autoimmune disease, blood lipid disorder, breast cysts, cachexia, cancer, cardiac restenosis, cardiovascular diseases, chronic inflammation, coronary heart disease, cystic fibrosis, degenerative disorder of the liver, diabetes, eczema, gastrointestinal disorder, heart disease, high triacylglycerol levels, hypertension, hyperactivity, immunological diseases, inhibiting tumor growth, inflammatory conditions, intestinal disorders, kidney dysfunction, leukemia, major depression, multiple sclerosis, neurodegenerative disorder, osteoarthritis, osteoporosis, peroxisomal disorder, preeclampsia, preterm birth, psoriasis, pulmonary disorder rheumatoid arthritis, risk of heart disease, or thrombosis.
  • a condition, disease, or disorder such as acne, acute inflammation, age related maculopathy, allergy, Alzheimer's, arthritis, asthma, at
  • the composition is used to increase the length of gestation of a fetus in the third trimester.
  • the composition is used to control blood pressure.
  • the composition is used to improve or maintain cognitive function.
  • the composition is used to improve or maintain memory.
  • the composition or dosage form can be administered into the body of a subject by any route compatible with the composition or dosage form.
  • a substance is considered to be “administered” if the substance is introduced into the body of the subject by the subject, or if another person, a machine, or a device introduces the substance into the body of the subject.
  • administering includes, e.g., self-administration, administration by others, and indirect administration.
  • continuous or “consecutive,” as used herein in reference to “administration,” means that the frequency of administration is at least once daily.
  • the frequency of administration can be greater than once daily and still be “continuous” or “consecutive,” e.g., twice or even three times daily, as long as the dosage levels as specified herein are not exceeded.
  • the means and methods for administration are known in the art and an artisan can refer to various pharmacologic references for guidance. For example, “Modern Pharmaceutics,” Banker & Rhodes, In forma Healthcare, USA, 4th ed. (2002); and “Goodman & Gilman's The Pharmaceutical Basis of Therapeutics,” McGraw-Hill Companies, Inc., New York, 10th ed. (2001) can be consulted.
  • subject means any subject, whether human or non-human, for whom diagnosis, prognosis, therapy, or administration of the composition or dosage form is desired.
  • Mammalian subjects include, but are not limited to, humans; domestic animals; farm animals; zoo animals; sport animals; pet animals such as dogs, cats, guinea pigs, rabbits, rats, mice, or horses; primates such as monkeys (e.g., cebus, rhesus, African green, patas, cynomolgus, and cercopithecus), apes, orangutans, baboons, gibbons, and chimpanzees; canids such as dogs and wolves; felids such as cats, lions, and tigers; equids such as horses, donkeys, and zebras; food animals such as cows, cattle, pigs, and sheep; ungulates such as deer and giraffe
  • the term subject also encompasses model animals, e.g., disease model animals.
  • the term subject includes valuable animals, either economically or otherwise, e.g., economically important breeding stock, racing animals, show animals, heirloom animals, rare or endangered animals, or companion animals.
  • the subject is a human subject. In certain embodiments, the subject is a non-human subject.
  • the composition can be administered as a "nutritional amount,” “therapeutically effective amount,” a “prophylactically effective amount,” a “therapeutic dose,” or a “prophylactic dose.”
  • a “nutritional amount” refers to an amount effective, at dosages and for periods of time necessary, to achieve a desired nutritional result.
  • a nutritional result can be, e.g., increased levels of a desirable fatty acid component in a subject.
  • a “therapeutically effective amount” or “therapeutic dose” refers to an amount effective, at dosages and for periods of time necessary, to achieve a desired therapeutic result.
  • a therapeutic result can be, e.g., lessening of symptoms, prolonged survival, improved mobility, and the like.
  • a therapeutic result need not be a “cure.”
  • a “prophylactically effective amount” or “prophylactic dose” refers to an amount effective, at dosages and for periods of time necessary, to achieve the desired prophylactic result. Typically, since a prophylactic dose is used in subjects prior to or at an earlier stage of disease, a prophylactically effective amount will be less than a therapeutically effective amount for treatment of an advanced stage of disease.
  • compositions, dosage form, or pharmaceutical composition can be administered to a subject, based on the amount of EPA or other fatty acid component of the microorganism, biomass, or microbial oil to be administered to the subject.
  • the terms "daily dosage,” “daily dosage level,” and “daily dosage amount” refer herein to the total amount of EPA or other fatty acid component administered per day (per 24 hour period).
  • administration of EPA to a subject at a daily dosage of 2 mg means that the subject receives a total of 2 mg of EPA on a daily basis, whether the EPA is administered as a single dosage form comprising 2 mg EPA, or alternatively, four dosage forms comprising 0.5 mg EPA each (for a total of 2 mg EPA).
  • the daily amount of EPA is administered in a single dosage form, or in two dosage forms.
  • the dosage forms of the present invention can be taken in a single application or multiple applications. For example, if four tablets are taken daily, each tablet comprising 0.5 mg EPA, then all four tablets can be taken once daily, or 2 tablets can be taken twice daily, or 1 tablet can be taken every 6 hours. In some embodiments, the daily dosage is about 100 mg to about 15 g of EPA.
  • the daily dosage is about 0.5 mg to about 250 mg, about 100 mg to about 250 mg, about 100 mg to about 500 mg, about 100 mg to about 1 g, about 1 g to about 2.5 g, about 1 g to about 5 g, about 1 g to about 10 g, about 1 g to about 15 g, about 5 g to about 10 g, about 5 g to about 15 g, about 10 g to about 15 g, about 100 mg to about 10 g, about 100 mg to about 5 g, or about 100 mg to about 2.5 g of EPA, DHA, or a combination thereof.
  • the composition is a dosage form that comprises about 0.5 mg to about 250 mg, 100 mg to about 250 mg, about 0.5 mg to about 500 mg, about 100 mg to about 500 mg, about 0.5 mg to about 1 g, or about 100 mg to about 1 g of EPA, DHA, or a combination thereof per dosage form.
  • Administration of the compositions or dosage forms of the present invention can be achieved using various regimens. For example, in some embodiments, administration occurs daily on consecutive days, or alternatively, occurs every other day (bi-daily). Administration can occur on one or more days.
  • compositions and dosage forms can be combined with other regimens used for treatment of the condition.
  • the method of the present invention can be combined with diet regimens (e.g., low carbohydrate diets, high protein diets, high fiber diets, etc.), exercise regimens, weight loss regimens, smoking cessation regimens, or combinations thereof.
  • diet regimens e.g., low carbohydrate diets, high protein diets, high fiber diets, etc.
  • exercise regimens e.g., low carbohydrate diets, high protein diets, high fiber diets, etc.
  • weight loss regimens e.g., smoking cessation regimens, or combinations thereof.
  • smoking cessation regimens e.g., smoking cessation regimens, or combinations thereof.
  • the method of the present invention can also be used in combination with other pharmaceutical products in the treatment of the condition.
  • the compositions or dosage forms of the present invention can be administered before or after other regimens or pharmaceutical products.
  • kits or packages containing one or more units of a composition of the invention.
  • Kits or packages can include units of a food product, pharmaceutical composition, cosmetic, or industrial composition comprising the microorganism, biomass, or microbial oil of the invention, or combinations thereof.
  • Kits or packages can also include an additive comprising the microorganism, biomass, or microbial oil of the invention, or combinations thereof for preparation of a food, cosmetic, pharmaceutical composition, or industrial composition.
  • the kit or package contains one or more units of a pharmaceutical composition to be administered according to the methods of the present invention.
  • the kit or package can contain one dosage unit, or more than one dosage unit (i.e., multiple dosage units). If multiple dosage units are present in the kit or package, the multiple dosage units can be optionally arranged for sequential administration.
  • kits of the present invention can optionally contain instructions associated with the units or dosage forms of the kits.
  • Such instructions can be in a form prescribed by a governmental agency regulating the manufacture, use or sale of pharmaceutical products, which notice reflects approval by the agency of the manufacture, use or sale for human administration to treat a condition or disorder.
  • the instructions can be in any form which conveys information on the use of the units or dosage forms in the kit according to the methods of the invention.
  • the instructions can be in the form of printed matter, or in the form of a pre-recorded media device.
  • a medical professional can determine that administration of one of the methods of the present invention is appropriate for the patient, or the physician can determine that the patient's condition can be improved by the administration of one of the methods of the present invention.
  • the physician can counsel the patient, for example, on the various risks and benefits associated with the regimen.
  • the patient can be provided full disclosure of all known and suspected risks associated with the regimen.
  • Such counseling can be provided verbally, as well as in written form.
  • the physician can provide the patient with literature materials on the regimen, such as product information, educational materials, and the like.
  • the present invention is directed to methods of educating consumers about the methods of treatment, the method comprising distributing the dosage forms with consumer information at a point of sale. In some embodiments, the distribution will occur at a point of sale having a pharmacist or healthcare provider.
  • consumer information can include, but is not limited to, an English language text, non-English language text, visual image, chart, telephone recording, website, and access to a live customer service representative.
  • consumer information will provide directions for use of the dosage forms according to the methods of the present invention, appropriate age use, indication, contraindications, appropriate dosing, warnings, telephone number or website address.
  • the method further comprises providing professional information to relevant persons in a position to answer consumer questions regarding use of the disclosed regimens according to the methods of the present invention.
  • professional information includes, but is not limited to, information concerning the regimen when administered according to the methods of the present invention that is designed to enable a medical professional to answer costumer questions.
  • a "medical professional,” includes, for example, a physician, physician assistant, nurse, nurse practitioner, pharmacist and customer service representative.
  • Isolation media consisted of: 500 ml of artificial seawater, 500 ml of distilled water, 1 g of glucose, 1 g of glycerol, 13 g of agar, 1 g of glutamate, 0.5 g of yeast extract, 0.5 g casein hydrolysate, 1 ml of a vitamin solution (100 mg/L thiamine, 0.5 mg/L biotin, 0.5 mg B ⁇ 2 ), 1 ml of a trace mineral solution (PII metals, containing per liter: 6.0 g FeCWHiO, 6.84 g H3BO 3 , 0.86 g MnCl 2 4H 2 0, 0.06 g ZnCl 2 , 0.026 CoCl 2 6H 2 0, 0.052 g NiS0 4 H 2 0, 0.002 g CuS0 4 5H 2 0 and 0.005 g Na 2 Mo0 4 2H 2 0), and 500 mg each of penicillin G and streptomycin sulfate.
  • the agar plates were incubated in the dark at 20-25°C. After 2-4 days the agar plates were examined under magnification, and colonies of cells were picked with a sterile toothpick and restreaked onto a fresh plate of media. Cells were repeatedly streaked onto fresh media until contaminated organisms were removed. Two of the isolated microorganisms were deposited under ATCC Accession Nos. PTA- 10212 and PTA- 10208.
  • PTA-10212 appeared as white, wet, smeared colonies without visible isolated sori. 101 131 PTA-10212 was grown on solid and liquid FFM, solid KMV, KMV slush (1%),
  • KMV broth, and MH broth to further examine growth characteristics.
  • PTA-10212 was observed to grow rapidly on KMV and MH. See, e.g., Porter D., 1989. Phylum Labyrinthiilomycota. In Margulis, L., Corliss, J.O., Melkonian, M., Chapman, D.J. (Eds.) Handbook of Protoctista, Jones and Bartlett, Boston, pp. 388-398 (KMV); Hyundai et al, Mycol. Res. 702:439-448 (1998) (MH); and U.S. Patent No. 5, 130,242 (FFM), each of which is incorporated herein by reference in its entirety.
  • PT A- 10212 was further examined using the flow-through technique, in which microscopic slides were prepared by suspending a small portion of an agar-grown colony in a drop of half-strength sea water. With this technique, primary sporangia were observed to be globose and approximately 10 ⁇ in diameter. Walls were very thin and remnants were not observed when binary division of the protoplast was initiated. Repeated binary division produced 8-16 smaller (4-5 ⁇ in diameter) secondary sporangia. The secondary sporangia remained quiescent for several hours before again releasing an amorphous protoplast.
  • the amorphous protoplast divided by pinching and pulling, initially producing typical dumbbell-shaped intermediate stages and finally resulting in 4-8 small globose bodies 2.5-2.8 ⁇ in diameter.
  • the latter rested for several minutes up to 1-2 hours, then changed shape (elongated) and turned into biflagellate zoospores, 2.3-2.5 x 3.7-3.9 ⁇ .
  • Zoospores were abundant and could be precisely measured when they came to rest. Zoospores then rounded off and started a new cycle of development.
  • the zoospores were larger than Sicyoidochytrium minutum and smaller than Ulkenia visurgensis.
  • PTA-10212 was further characterized based on the similarity of its 18s rRNA gene to that of known species. Genomic DNA was prepared from PTA-10212 by standard procedures. See, for example, Sambrook J. and Russell D. 2001. Molecular cloning: A laboratory manual, 3rd edition. Cold Spring Harbor Laboratory Press, Cold Spring Harbor, New York. Briefly: (1) 500 xL of cells were centrifuged from mid-log culture.
  • the cells were re-centrifuged, and all traces of liquid were removed from the cell pellet with a small-bore tip; (2) pellets were resuspended with 200 ⁇ ⁇ lysis buffer (20 mM Tris pH 8.0, 125 ⁇ g/mL Proteinase K, 50 niM NaCl, 10 niM EDTA pH 8.0, 0.5% SDS); (3) cells were lysed at 50°C for 1 hour; (4) the lysis mixture was pipetted into phase-lock gel (PLG-Eppendorf) 2 mL tubes; (5) equal volume of P:C:I was added and allowed to mix for 1.5 hours; (6) the tubes were centrifuged at 12,000 x g for 5 minutes; (7) the aqueous phase was removed from above the gel within the PLG tube and an equal volume of chloroform was added to the aqueous phase, and mixed for 30 minutes; (8) the tubes were centrifuged at 14,000 x g for approximately 5 minutes; (9) the top layer
  • the PCR amplification of the 18s rRNA gene was carried out with primers previously described (Honda et. al, J. Euk. Micro. 46(6): 637-647 (1999).
  • the PCR conditions with chromosomal DNA template were as follows: 0.2 ⁇ dNTPs, 0.1 ⁇ each primer, 8% DMSO, 200 ng chromosomal DNA, 2.5 U Herculase® II Fusion DNA Polymerase (Stratagene), and Herculase® buffer (Stratagene) in a 50 ⁇ , total volume.
  • the PCR Protocol included the following steps: (1) 95°C for 2 minutes; (2) 95°C for 35 seconds; (3) 55°C for 35 seconds; (4) 72°C for 1 minute and 30 seconds; (5) repeat steps 2-4 for 30 cycles; (6) 72°C for 5 minutes; and (7) hold at 4°C.
  • PCR amplification yielded a distinct DNA product with the expected size using chromosomal template described above.
  • the PCR product was cloned into the vector pJET1.2/blunt (Fermentas) according to the manufacturer's instructions, and the insert sequence was determined using supplied standard primers.
  • Thranstochytrium pachydermum and Thraustochytrium aggregatum with moderate support The sporangia of T. pachydermum have very thick cell walls. T. aggregatum forms clearly visible clumps of sori that are opaque. PTA-10212 shows neither of these characteristics. The presence of many amoeboid cells has been described in other taxa, such as Ulkenia, T. gaertnerium, A. limiacinum, and S. mangrovei; however, the descriptions associated with those taxa differ from the observed characteristics of the isolate. Moreover, PTA-10212 did not show phylogenetic affinity towards any of these taxa.
  • Table 3 shows a comparison of the 18s rRNA sequence from the microorganism deposited under ATCC Accession No. PTA-10212 to DNA sequences in the National Center for Biotechnology Information (NCBI) electronic database. The percent identity was determined using two different calculations. “Calculation #1” takes into consideration any “gaps” that occur in the sequences, either from non-homologous regions or partial sequence (AlignX-VectorNTI default settings). “Calculation #2” does not include calculated penalties for gaps (AlignX-VectorNTI "IDENTITY” matrix setting). Table 3: Comparison of 1 8s rRNA Sequences
  • 18s rRNA gene sequence (SEQ ID NO: l) from the microorganism deposited under ATCC Accession No. PTA-10212 is related, though not identical, to 18s rRNA gene sequences available in the NCBI database. It is generally recognized that organisms can have closely related 18s rRNA gene sequences while belonging to a different genus or species.
  • ATCC Accession No. PTA-10212 is believed to represent a new Thraustochytrium species and is therefore also designated as Thraustochytrium sp, ATCC PTA-10212.
  • PTA-9695 was identified as a sub-isolate (an individual cell isolated from a culture and maintained as a new separate and distinct culture) of the microorganism deposited under ATCC Accession No. PTA-9695 (“PTA-9695”), described in U.S. Appl. No. 12/407,687 and PCT/US2009/001720, each of which is incorporated herein by reference in its entirety.
  • PTA-10208 shares taxonomic characteristics with PTA-9695.
  • PTA-9695 was found to have biflagellate zoospores at discharge that swim actively away from the mature sporangium, wall remnants of which were clearly visible (in phase contrast) after spore release.
  • PTA-9695 sporangia measured 12.5 ⁇ to 25 ⁇ in diameter, and zoospores were 2.5 ⁇ to 2.8 ⁇ x 4.5 ⁇ to 4.8 ⁇ in size. There were 8 to 24 spores per individual PTA-9695 sporangium.
  • the 18s rRNA sequence published for Thraustochytrium aggregation is a partial sequence, with an approximately 71 DNA nucleotide gap in the middle of the sequence.
  • PTA-9695 is believed to represent a new Schizochytrium species.
  • the sub- isolate PTA- 10208 is also designated as Schizochytrium sp. ATCC PTA- 10208.
  • PTA-10212 produced a dry cell weight of 26.2 g/L after 138 hours of culture in a 10 L fermentor volume.
  • the lipid yield was 7.9 g/L; the omega- 3 yield was 5.3 g/L; the EPA yield was 3.3 g/L; and the DHA yield was 1.8 g/L.
  • the fatty acid content was 30.3% by weight; the EPA content was 41.4% of fatty acid methyl esters (FAME); and the DHA content was 26.2% of FAME.
  • the lipid productivity was 1.38 g/L/day, and the omega-3 productivity was 0.92 g/L/day under these conditions, with 0.57 g/L/day EPA productivity and 0.31 g/L/day DHA productivity.
  • PTA-10212 produced a dry cell weight of 38.4 g/L after 189 hours of culture in a 10 L fermentor volume.
  • the lipid yield was 18 g/L; the omega- 3 yield was 12 g/L; the EPA yield was 5 g/L; and the DHA yield was 6.8 g/L.
  • the fatty acid content was 45% by weight; the EPA content was 27.8% of FAME; and the DHA content was 37.9% of FAME.
  • the lipid productivity was 2.3 g/L/day, and the omega-3 productivity was 1.5 g/L/day under these conditions, with 0.63 g/L/day EPA productivity and 0.86 g/L/day DHA productivity.
  • PTA-10212 produced a dry cell weight of 13 g/L after 189 hours of culture in a 10 L fermentor volume.
  • the lipid yield was 5.6 g/L; the omega-3 yield was 3.5 g/L; the EPA yield was 1.55 g/L; and the DHA yield was 1.9 g/L.
  • the fatty acid content was 38% by weight; the EPA content was 29.5% of FAME; and the DHA content was 36% of FAME.
  • the lipid productivity was 0.67 g/L/day, and the omega-3 productivity was 0.4 g/L/day under these conditions, with 0.20 g/L/day EPA productivity and 0.24 g/L/day DHA productivity.
  • the fatty acid content was 42.4% - 53% by weight; the EPA content was 9.8% - 22% of FAME; and the DHA content was 38.1 % - 43.6% of FAME.
  • the lipid productivity was 1.9 g/L/day - 3.2 g/L/day, and the omega-3 productivity was 1.2 g/L/day - 1.7 g/L/day under these conditions, with 0.31 g/L/day - 0.41 g/L/day EPA productivity and 0.72 g/L/day - 1.4 g/L/day DHA productivity.
  • PTA- 10208 produced a dry cell weight of 95 g/L after 200 hours of culture in a 10 L fermentor volume.
  • the lipid yield was 53.7 g/L; the omega-3 yield was 37 g/L; the EPA yield was 14.3 g/L; and the DHA yield was 21 g/L.
  • the fatty acid content was 57% by weight; the EPA content was 27.7% of FAME; and the DHA content was 39.1 % of FAME.
  • the lipid productivity was 6.4 g/L/day, and the omega-3 productivity was 4.4 g/L/day under these conditions, with 1.7 g/L/day EPA productivity and 2.5 g/L/day DHA productivity.
  • PTA-10208 produced a dry cell weight of 56 g/L after 139 hours of culture in a 10 L fermentor volume.
  • the lipid yield was 53 g/L; the omega-3 yield was 34 g/L; the EPA yield was 1 1.5 g/L; and the DHA yield was 22 g/L.
  • the fatty acid content was 58% by weight; the EPA content was 21.7% of FAME; and the DHA content was 41.7% of FAME.
  • the lipid productivity was 9.2 g/L/day, and the omega-3 productivity was 5.9 g/L/day under these conditions, with 2 g/L/day EPA productivity and 3.8 g/L/day DHA productivity.
  • PTA-10208 produced a dry cell weight of 93.8 g/L after 167 hours of culture in a 2000 L fermentor volume.
  • the lipid yield was 47.2 g/L; the omega-3 yield was 33.1 g/L; the EPA yield was 10.5 g/L; and the DHA yield was 20.4 g/L.
  • the fatty acid content was 50.6%) by weight; the EPA content was 23% of FAME; and the DHA content was 42.6% of FAME.
  • the lipid productivity was 6.8 g/L/day, and the omega-3 productivity was 4.7 g/L/day under these conditions, with 1.5 g/L/day EPA productivity and 2.9 g/L/day DHA productivity.
  • PTA-10208 produced a dry cell weight of 105 g/L after 168 hours of culture in a 2000 L fermentor volume.
  • the lipid yield was 46.4g/L; the omega-3 yield was 33 g/L; the EPA yield was 10.7 g/L; and the DHA yield was 20.3 g/L.
  • the fatty acid content was 43.9% by weight; the EPA content was 24% of FAME; and the DHA content was 43.7% of FAME.
  • the lipid productivity was 6.6 g/L/day, and the omega-3 productivity was 4.7 g/L/day under these conditions, with 1.5 g/L/day EPA productivity and 2.9 g/L/day DHA productivity.
  • PTA-10208 produced a dry cell weight of 64.8 g/L after 168 hours of culture in a 2000 L fermentor volume.
  • the lipid yield was 38.7 g/L; the omega-3 yield was 29.9 g/L; the EPA yield was 8.5 g/L; and the DHA yield was 16.7 g/L.
  • the fatty acid content was 59.6% by weight; the EPA content was 23% of FAME; and the DHA content was 42.3%> of FAME.
  • the lipid productivity was 5.53 g/L/day, and the omega-3 productivity was 3.8 g/L/day under these conditions, with 1.2 g/L/day EPA productivity and 2.3 g/L/day DHA productivity.
  • Fatty acids in the extracted crude lipid were also quantified by transesterification and quantified using GC/FID analysis of the resultant FAME.
  • the weight percent of all neutral lipids (NL) and free fatty acids (FFA) were determined in the extracted crude lipid using normal phase HPLC with ELSD and atmospheric pressure chemical ionization-MS (APCI-MS) identification.
  • the method separates and quantifies sterol esters (SE), TAG, free fatty acids (FFA), 1,3-diacylglycerols (1, 3-D AG), sterols, 1,2-diacylglycerols (1 ,2-DAG), and monoacylglycerols (MAG). Results are shown in Tables 4 and 5, below.
  • TAG and phospholipids were isolated from the crude oils extracted from the four samples of biomass (PTA-10208 Sample #1 ; PTA-10208 Sample #2; PTA-10212 Sample #1 ; and PTA-10212 Sample #2).
  • TAG was isolated using low pressure flash chromatography and PL was isolated using solid phase extraction (SPE). The identity of each isolated fraction was confirmed by thin layer chromatography (TLC).
  • TLC thin layer chromatography
  • the fatty acid profiles of the isolated TAG and PL fractions were determined following direct transesterification using GC-FID as FAME. Results are shown in Tables 6 and 7, below.
  • Crude Oil Extraction - Crude oil was extracted from samples of freeze-dried biomass using solvent grinding. For example, approximately 3 grams of biomass was weighed into a Swedish tube. Three ball bearings and 30 mL of hexane were added to the Swedish tube, which was sealed with a neoprene stopper and placed in a shaker for 2 hours. The resultant slurry was filtered using a Buchner funnel and Whatman filter paper. The filtered liquid was collected, the solvent removed under vacuum, and the amount of remaining crude lipid determined gravimetrically.
  • Fatty Acid Analysis The samples of biomass, extracted crude lipid, and isolated lipid classes were analyzed for fatty acid composition as FAME. Briefly, freeze-dried biomass and isolated lipid classes were weighed directly into a screw cap test tubes, while samples of the crude oil were dissolved in hexane to give a concentration of approximately 2 mg/mL. Toluene, containing internal standard, and 1.5 N HC1 in methanol was added to each tube. The tubes were vortexed, then capped and heated to 100° C for 2 hours. The tubes were allowed to cool, and saturated NaCl in water was added. The tubes were vortexed again and centrifuged to allow the layers to separate.
  • the fatty acids were then eluted with 15 mL of 2% acetic acid (HO Ac) in ether, which was discarded.
  • the PL portion was eluted with 15 mL of 6: 1 Methanol : Chloroform, which was collected, dried under nitrogen, and weighed.
  • Flash Chromatography - Flash chromatography was used to separate the lipid classes present in the crude oil. Approximately 200 mg of crude oil dissolved in hexane was injected onto the head of the column. The chromatography system utilized Silica Gel 60 (EMD Chemical, Gibbstown, NJ) with mobile phase composed of Petroleum Ether and Ethyl Acetate at 5 mL/min (Tables 6-7) or 3 mL/min (Tables 8-13). A step gradient was used to selectively elute each lipid class from the column. The mobile phase gradient started from 100% petroleum ether and finished with 50% ethyl acetate.
  • Fractions were collected in 10 mL test tubes using a Gilson FC 204 large-bed fraction collector (Gilson, Inc., Middleton, WI). Each tube was analyzed by thin layer chromatography (TLC) and the tubes containing individual lipid classes (as judged by single spots on TLC plate with expected retention factor (Rf)) were pooled, concentrated to dryness, and weighed. The total fraction content was then determined gravimetrically.
  • Gilson FC 204 large-bed fraction collector Gilson, Inc., Middleton, WI.
  • the plates were eluted using a solvent system consisting of petroleum ether : ethyl ether : acetic acid (80:20:1) and were visualized using iodine vapor.
  • the Rf values of each spot were then compared with reported literature values for each lipid class.
  • TAG and PL fractions The isolated TAG and PL fractions were analyzed for fatty acid composition as fatty acid methyl esters (FAME).
  • the TAG fractions were dissolved in hexane to give a concentration of approximately 1 -2 mg/mL. 1 mL aliquots of the solutions were concentrated to dryness under nitrogen. Toluene, containing internal standard, and 1.5 N HC1 in methanol was added to each tube. The tubes were vortex ed, then capped and heated to 100° C for 2 hours. Internal standard and HC1 methanol were added directly to the tubes containing the PL fraction and heated. The tubes were allowed to cool, and saturated NaCl in water was added.
  • FAME fatty acid methyl esters
  • the tubes were vortexed again and centrifuged to allow the layers to separate. A portion of the organic layer was then placed in a GC vial and analyzed by GC-FID. FAMEs were quantified using a 3 -point calibration curve generated using Nu-Check-Prep GLC 502B Reference Standard (NuCheck, Elysian, MN). Fatty acids present in the extract were expressed as mg/g and as a % of FAME.
  • Sample #1 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 28.6 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 55.0 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 53.2% (as SUM of FAME) using GC with FID detection, while 52.0% (wt/wt) lipid was extracted from the dry biomass, giving a 97.8% recovery of total lipid. The crude lipid was determined to be 91.9% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were C16:0 (182.5 mg/g), C20:5 n-3 (186.8 mg/g), and C22:6 n-3 (423.1 mg/g).
  • the lipid class profile of the extracted crude lipid was determined by weighing
  • the crude lipid contained 0.2% sterol esters (SE), 95.1 % TAG, 0.4% sterols, and 0.5% 1,2-diacylglycerol (DAG). 5% of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
  • SE sterol esters
  • DAG 1,2-diacylglycerol
  • TAG Isolated TAG from this sample as determined by flash chromatography made up approximately 92.4% of the crude oil. PL was not detected by weight or TLC after SPE isolation. The major fatty acids (>50 mg/g) contained in the TAG were C I 6:0 (189 mg/g), C20:5 n-3 (197 mg/g), and C22:6 n-3 (441 mg/g). PTA-10208 Sample #2
  • Sample #2 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 32.0 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 60.1 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 52.4% (as SUM of FAME) using GC with FID detection, while 48.0% (wt/wt) lipid was extracted from the dry biomass, giving a 91.7% recovery of total lipid. The crude lipid was determined to be 95.3% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were C16:0 (217.5 mg/g), C20:5 n-3 (169.3 mg/g), and C22:6 n-3 (444.1 mg/g).
  • the lipid class profile of the extracted crude lipid was determined by weighing
  • the crude lipid contained 0.2% SE, 95.7% TAG, 0.3% sterols, and 0.7% 1,2-DAG.
  • 5.1 % of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
  • the major fatty acids (>50mg/g) contained in the TAG were C I 6:0 (218 mg/g), C20:5 n-3 (167 mg/g) and C22:6 n-3 (430 mg/g).
  • PTA-10208 (Sample PTA-10208 #3) was analyzed using HPLC/ELSD/MS. A total of 98.38%o of lipids were recovered, with the sterol ester (SE) fraction accounting for 0.32%, the TAG fraction accounting for 96.13%, the 1 ,3-diacylglycerol (DAG) fraction accounting for 0.22%, the 1 ,2-DAG fraction accounting for 0.78%, and the sterol fraction accounting for 0.93%.
  • SE sterol ester
  • DAG 1 ,3-diacylglycerol
  • sterol fraction accounting for 0.93%.
  • Sample #1 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 27.0 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 52.5 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 38.3% (as SUM of FAME) using GC with FID detection, while 36.3% (wt/wt) lipid was extracted from the dry biomass, giving a 94.6% recovery of total lipid. The crude lipid was determined to be 83.2% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were CI 6:0 (328.5 mg/g), C20:5 n-3 (90.08 mg/g), and C22:6 n-3 (289.3 mg/g).
  • the lipid class profile of the extracted crude lipid was determined by weighing
  • the crude lipid contained 0.2% SE, 64.2% TAG, 1.9% FFA, 2.8% 1 ,3-DAG, 1.4% sterols, 18.8% 1 ,2-DAG, and 0.5% MAG.
  • 3.4% of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
  • Isolated TAG from this sample made up approximately 49.8% of the crude oil.
  • Isolated PL made up approximately 8.1 % of the crude oil.
  • the major fatty acids (>50mg/g) contained in the TAG fraction are C16:0 (400 mg/g), C20:5 n-3 (91 mg/g), and C22:6 n-3 (273 mg/g).
  • the major fatty acids (>50mg/g) contained in the PL fraction are C16:0 (98 mg/g), C20:5 n-3 (33 mg/g), and C22:6 n-3 (227 mg/g).
  • the lipid class profile of the extracted crude lipid was determined by weighing
  • the crude lipid contained 0.2% SE, 58.2% TAG, 2.3% FFA, 3.4% 1,3-DAG, 1.7% sterols, 23.4% 1 ,2-DAG, and 0.6% MAG.
  • 3.3% of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
  • Isolated TAG from this sample made up approximately 51.9% of the crude oil.
  • Isolated PL made up approximately 8.8% of the crude oil.
  • the major fatty acids (>50mg/g) contained in the TAG fraction are CI 6:0 (402 mg/g), C20:5 n-3 (92 mg/g), and C22:6 n-3 (245 mg/g).
  • the major fatty acids (>50mg/g) contained in the PL fraction are C16:0 (121 mg/g), C20:5 n-3 (48 mg/g), and C22:6 n-3 (246 mg/g).
  • Fatty FAME FAME FAME FAME FAME FAME FAME FAME FAME FAME FAME FAME Acid (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g)
  • the lipid content of the biomass for PTA-10212 Sample #3 was estimated to be
  • Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
  • PTA-10212 Sample #4 contained approximately 23% lipid determined as the sum of FAME, of which 107% was recovered using hexane extraction. After fractionation using flash chromatography, approximately 42% of the crude oil was isolated as TAG, 18% was isolated as DAG. The crude oil contained 275 mg/g DHA and 209 mg/g EPA. The isolated TAG contained 296 mg/g DHA and 205 mg/g EPA. The isolated DAG fraction contained 245 mg/g DHA and 219 mg/g EPA. The total fatty acid profiles of the biomass, extracted crude oil, and isolated fractions are shown below in Table 10 (mg/g) and Table 1 1 (%FAME).
  • Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
  • Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
  • a sample of crude oil was extracted from a biomass of PTA-10212 using the
  • the sample was prepared by dissolving 240 mg of crude oil in 600 ⁇ , of hexane and applying to the head of the column. After fractionation of the sample using flash chromatography, the combined weights of all the fractions was 240 mg giving a 100% recovery.
  • the sterol ester fraction accounted for 0.9%
  • the TAG fraction accounted for 42.6%.
  • the free fatty acid (FFA) fraction accounted for 1.3%
  • the sterol fraction accounted for 2.2%
  • the DAG fraction accounted for 41.6%.
  • the total fatty acid profiles of the FRIOLEX® crude oil and isolated fractions are shown below in Table 12 and Table 13 calculated as mg/g and % FAME, respectively.
  • Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
  • each TAG isomer present in the extracted crude lipid was determined for each of samples PTA- 10208 Sample #1, PTA- 10208 Sample #2, PTA-10212 Sample #1 , PTA-10212 Sample #2, and PTA-10212 Sample #3, PTA-10212 Sample #4, and PTA-10212 Sample #5 from Example 3 using non-aqueous reversed phase HPLC separation and APCI-MS detection.
  • the crade lipid isolated from PTA-10212 Sample #2 was prepared for TAG analysis prepared for TAG analysis by weighing 3.6 mg of oil into an HPLC vial and diluting with 1 mL of hexane.
  • TAG fraction of PTA-10212 Sample #3 was prepared in hexane and analyzed by HPLC/APCl/MS to determine the identities of individual TAG isomers.
  • Table 1 8 Identification of TAG Species in PTA- 10212 Sample #3
  • TAG fraction of PTA-10212 Sample #4 was prepared in hexane and analyzed by HPLC/APCI/MS to determine the identities of individual TAG isomers.
  • TAG fraction of PTA-10212 Sample #5 was prepared in hexane and analyzed by HPLC/APCI/MS to determine the identities of individual TAG isomers. Table 20: Identification of TAG Species in PTA- 10212 Sample #5
  • Crude oils were further processed via refining, bleaching, and deodorizing to obtain refined oils.
  • the refined oils were diluted with high oleic sunflower oil to obtain final oils with a DHA content of approximately 400 mg/g.
  • Individual lipid classes were isolated and the fatty acid profiles of each class was determined using GC-FID as FAME.
  • DHA was present in a PTA-10212 Final Oil at 41.63% and 366.9 mg/g, while EPA was present at 16.52%. Individual fatty acid profiles were determined and are summarized in Table 29.
  • ND Not Detected EXAMPLE 6
  • TAGs triacylglycerides

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • General Health & Medical Sciences (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Food Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Animal Behavior & Ethology (AREA)
  • Veterinary Medicine (AREA)
  • Public Health (AREA)
  • Medicinal Chemistry (AREA)
  • Animal Husbandry (AREA)
  • Epidemiology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Birds (AREA)
  • Mycology (AREA)
  • Biomedical Technology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Nutrition Science (AREA)
  • Virology (AREA)
  • Cell Biology (AREA)
  • Physiology (AREA)
  • Sustainable Development (AREA)
  • Molecular Biology (AREA)
  • Emergency Medicine (AREA)
  • Dermatology (AREA)
  • Botany (AREA)
  • Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)

Abstract

The present invention is directed to isolated microorganisms as well as strains and mutants thereof, biomasses, microbial oils, compositions, and cultures; methods of producing the microbial oils, biomasses, and mutants; and methods of using the isolated microorganisms, biomasses, and microbial oils.

Description

EICOSAPENTAENOIC ACID-PRODUCING MICROORGANISMS, FATTY ACID COMPOSITIONS, AND METHODS OF MAKING AN D USES THE REOF
BACKGROUND OF THE INVENTION Field of the Invention
[0001] The present invention is directed to isolated microorganisms as well as strains and mutants thereof, biomasses, microbial oils, compositions, and cultures; methods of producing the microbial oils, biomasses, and mutants; and methods of using the isolated microorganisms, biomasses, and microbial oils.
Background Art
[0002] Fatty acids are classified based on the length and saturation characteristics of the carbon chain. Fatty acids are termed short chain, medium chain, or long chain fatty acids based on the number of carbons present in the chain, are termed saturated fatty acids when no double bonds are present between the carbon atoms, and are termed unsaturated fatty acids when double bonds are present. Unsaturated long chain fatty acids are monounsaturated when only one double bond is present and are polyunsaturated when more than one double bond is present.
[0003] Polyunsaturated fatty acids (PUFAs) are classified based on the position of the first double bond from the methyl end of the fatty acid: omega-3 (n-3) fatty acids contain a first double bond at the third carbon, while omega-6 (n-6) fatty acids contain a first double bond at the sixth carbon. For example, docosahexaenoic acid ("DHA") is an omega-3 long chain polyunsaturated fatty acid (LC-PUFA) with a chain length of 22 carbons and 6 double bonds, often designated as "22:6 n-3." Other omega-3 LC-PUFAs include eicosapentaenoic acid ("EPA"), designated as "20:5 n-3," and omega-3 docosapentaenoic acid ("DPA n-3"), designated as "22:5 n-3." DHA and EPA have been termed "essential" fatty acids. Omega-6 LC-PUFAs include arachidonic acid ("ARA"), designated as "20:4 n-6," and omega-6 docosapentaenoic acid ("DPA n-6"), designated as "22:5 n-6."
[0004] Omega-3 fatty acids are biologically important molecules that affect cellular physiology due to their presence in cell membranes, regulate production and gene expression of biologically active compounds, and serve as biosynthetic substrates. Roche, H. M., Proc. Nutr. Soc. 58: 397-401 (1999). DHA, for example, accounts for approximately 15%-20% of lipids in the human cerebral cortex, 30%-60% of lipids in the retina, is concentrated in the testes and sperm, and is an important component of breast milk. Berge, J. P., and Barnathan, G.. Adv. Biochem. Eng. Biotechnol. 9(5:49-125 (2005). DHA accounts for up to 97% of the omega-3 fatty acids in the brain and up to 93% of the omega-3 fatty acids in the retina. Moreover, DHA is essential for both fetal and infant development as well as maintenance of cognitive functions in adults. Id. Because omega-3 fatty acids are not synthesized de novo in the human body, these fatty acids must be derived from nutritional sources.
[0005] Flaxseed oil and fish oils are considered good dietary sources of omega-3 fatty acids. Flaxseed oil contains no EPA, DHA, DPA, or ARA but rather contains linolenic acid (C I 8:3 n-3), a building block enabling the body to manufacture EPA. There is evidence, however, that the rate of metabolic conversion can be slow and variable, particularly among those with impaired health. Fish oils vary considerably in the type and level of fatty acid composition depending on the particular species and their diets. For example, fish raised by aquaculture tend to have a lower level of omega-3 fatty acids than those in the wild. Furthermore, fish oils carry the risk of containing environmental contaminants and can be associated with stability problems and a fishy odor or taste.
[0006] Thraustochytrids are microorganisms of the order Thraustochytriales.
Thraustochytrids include members of the genus Schizochytrium and Thraustochytrium and have been recognized as an alternative source of omega-3 fatty acids, including DHA and EPA. See U.S. Patent No. 5,130,242. Oils produced from these marine heterotrophic microorganisms often have simpler polyunsaturated fatty acid profiles than corresponding fish or microalgal oils. Lewis, T.E., Mar. Biotechnol. I 580-587 (1999). Strains of thraustochytrid species have been reported to produce omega-3 fatty acids as a high percentage of the total fatty acids produced by the organisms. U.S. Patent No. 5,130,242; Huang, J. et al., J. Am. Oil. Chem. Soc. 78: 605-610 (2001); Huang, J. et al., Mar. Biotechnol. 5: 450-457 (2003). However, isolated thraustochytrids vary in the identity and amounts of LC-PUFAs produced, such that some previously described strains can have undesirable levels of omega-6 fatty acids and/or can demonstrate low productivity in culture. As such, a continuing need exists for the isolation of microorganisms demonstrating high productivity and desirable LC-PUFA profiles.
BRIEF SUMMARY OF THE INVENTION
[0007] The present invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA- 10212.
[00081 The present invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA-10212.
[0009J The present invention is directed to an isolated microorganism comprising an 18s rRNA comprising a polynucleotide sequence of SEQ ID NO: l or a polynucleotide sequence having at least 94% identity to SEQ ID NOT .
|001 ] The present invention is directed to an isolated microorganism comprising an 18s rRNA polynucleotide sequence that has at least 94% identity to an 18s rRNA polynucleotide sequence of the microorganism deposited under ATCC Accession No.
PTA-10212.
1001 1 ] The present invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10% by weight eicosapentaenoic acid.
[0012] The present invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10% by weight eicosapentaenoic acid.
[0013] The present invention is directed to an isolated microorganism that produces a triacylglycerol fraction, wherein eicosapentaenoic acid content of the triacylglycerol fraction is at least about 12% by weight.
[0014] In some embodiments, the isolated microorganism of the invention is a mutant strain.
[0015] The present invention is directed to an isolated microorganism deposited under
ATCC Accession No. PTA-10212, PTA- 10213, PTA- 10214, PTA- 10215. PTA-10208, PTA- 10209, PTA- 10210, or PTA- 1021 1.
[0016] The present invention is directed to a biomass comprising any of the microorganisms of the invention or mixtures thereof. [0017] The present invention is directed to an isolated biomass, wherein at least about
20% by weight of a dry cell weight of the biomass are fatty acids, wherein more than about 10% by weight of fatty acids is eicosapentaenoic acid, and wherein the fatty acids comprise less than about 5% by weight each of arachidonic acid and docosapentaenoic acid n-6. In some embodiments, at least about 25% by weight of the fatty acids is docosahexaenoic acid.
[0018] In some embodiments, the present invention is directed to an isolated biomass comprising triacylglycerol, wherein at least about 12% by weight of triacylglycerol is eicosapentaenoic acid.
[0019] In some embodiments, the present invention is directed to any of the isolated biomasses of the invention wherein the fatty acids further comprise less than about 5% by weight each of oleic acid, linoleic acid, linolenic acid, eicosenoic acid, and erucic acid.
[0020] The present invention is directed to an isolated culture comprising any of the microorganisms of the invention or mixtures thereof.
[0021] The present invention is directed to a food product, cosmetic, or pharmaceutical composition for a non-human animal or human, comprising any of the microorganisms or biomasses of the invention or mixtures thereof.
[0022] The present invention is directed to a microbial oil comprising at least about 20% by weight eicosapentaenoic acid and less than about 5% by weight each of arachidonic acid, docosapentaenoic acid n-6, oleic acid, linoleic acid, linolenic acid, eicosenoic acid, erucic acid, and stearidonic acid. In some embodiments, the microbial oil further comprises at least about 25% by weight docosahexaenoic acid.
[0023] The present invention is directed to a microbial oil comprising a triacylglycerol fraction of at least about 10% by weight, wherein at least about 12% by weight of the fatty acids in the triacylglycerol fraction is eicosapentaenoic acid, wherein at least about 25% by weight of the fatty acids in the triacylglycerol fraction is docosahexaenoic acid, and wherein less than about 5% by weight of the fatty acids in the triacylglycerol fraction is arachidonic acid.
[0024] The present invention is directed to a food product, cosmetic, or pharmaceutical composition for a non-human animal or human, comprising any of the microbial oils of the invention. In some embodiments, the food product is an infant formula. In some embodiments, the infant formula is suitable for premature infants. In some embodiments, the food product is a milk, a beverage, a therapeutic drink, a nutritional drink, or a combination thereof. In some embodiments, the food product is an additive for the non- human animal or human food. In some embodiments, the food product is a nutritional supplement. In some embodiments, the food product is an animal feed. In some embodiments, the animal feed is an aquaculture feed. In some embodiments, the animal feed is a domestic animal feed, a zoological animal feed, a work animal feed, a livestock feed, or a combination thereof.
[0025] The present invention is directed to a method for producing a microbial oil comprising omega-3 fatty acids, the method comprising: growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce an oil comprising omega-3 fatty acids. In some embodiments, the method further comprises extracting the oil.
[0026] The present invention is directed to a method for producing a microbial oil comprising omega-3 fatty acids, the method comprising extracting an oil comprising omega-3 fatty acids from any of the biomasses of the invention. In some embodiments, the microbial oil is extracted using an organic solvent extraction process, for example hexane extraction. In some embodiments, the microbial oil is extracted using a solventless extraction process.
[0027] The present invention is directed to a microbial oil produced by a method of the invention.
[0028] The present invention is directed to a method for producing a biomass of the invention, comprising: growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce a biomass.
[0029] The present invention is directed to a biomass produced by a method of the invention.
[0030] The present invention is directed to a method for producing a mutant strain of the invention, comprising: mutagenizing any of the microorganisms of the invention, and isolating the mutant strain.
[0031 ] The present invention is directed to use of any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, for the manufacture of a medicament for treatment of inflammation or a condition related thereto. [0032] The present invention is directed to use of any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, for treatment of inflammation or a condition related thereto.
[0033] The present invention is directed to any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, for use in treatment of inflammation or a condition related thereto.
[0034] The present invention is directed to a method for treating inflammation or a condition related thereto in a subject in need thereof, comprising administering to the subject any of the isolated microorganisms, biomasses, or microbial oils of the invention, or mixtures thereof, and a pharmaceutically acceptable carrier.
DETAILED DESCRIPTION OF THE INVENTION
[0035] The present invention is directed to isolated microorganisms, as well as strains and mutants thereof, as well as biomasses, microbial oils, compositions, and cultures thereof. The present invention is directed to methods of producing microbial oils, biomasses, and mutants from the microorganisms of the invention, and methods of using the microorganisms, biomasses, and microbial oils. The microorganisms described herein are highly productive and produce unique fatty acid profiles, characterized in part by high levels of omega- 3 fatty acids, in particular high levels of EPA.
Microorganisms
[0036] The invention is directed to isolated microorganisms and strains derived therefrom. A strain that is "derived" from an isolated microorganism of the invention can be a natural or artificial derivative such as, for example, a mutant, variant, or recombinant strain. The term "isolated" as used herein does not necessarily reflect the extent to which an isolate has been purified, but indicates isolation or separation from a native form or native environment. An isolate can include, but is not limited to, an isolated microorganism, an isolated biomass, an isolated culture, an isolated microbial oil, and an isolated sequence (such as an isolated polynucleotide sequence disclosed herein). The term "microorganism" as used herein includes, but is not limited to, the terms "microalgae," "thraustochytrid," and taxonomic classifications associated with any of the deposited microorganisms described herein. The terms "Thraustochytriales," "thraustochytrid," "Schizochytrium," and " Thraustochytrium" as used in reference to any of the microorganisms of the invention, including the deposited microorganisms described herein, are based on present taxonomic classifications including available phylogenetic information and are not intended to be limiting in the event that the taxonomic classifications are revised after the filing date of the present application.
[0037] In some embodiments, the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA-10212. The isolated microorganism associated with ATCC Accession No. PTA-10212 is also known herein as Thraustochytrium sp. ATCC PTA-10212. The isolated microorganism associated with ATCC Accession No. PTA-10212 was deposited under the Budapest Treaty on July 14, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 20110-2209. In some embodiments, the invention is directed to an isolated strain deposited under ATCC Accession No. PTA-10212.
[0038] In some embodiments, the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10212 or a strain derived therefrom. The characteristics of the species deposited under ATCC Accession No. PTA-10212 can include its growth and phenotypic properties (examples of phenotypic properties include morphological and reproductive properties), its physical and chemical properties (such as dry weights and lipid profiles), its gene sequences, and combinations thereof, in which the characteristics distinguish the species over previously identified species. In some embodiments, the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA-10212, wherein the characteristics include an 18s rRNA comprising the polynucleotide sequence of SEQ ID NOT or a polynucleotide sequence having at least 94%, 95%, 96%, 97%, 98%, or 99% identity to SEQ ID NOT , the morphological and reproductive properties of the species deposited under ATCC Accession No. PTA- 10212, and the fatty acid profiles of the species deposited under ATCC Accession No. PTA-10212. hi some embodiments, isolated microorganisms of the invention have phenotypic properties substantially identical to those of the microorganism deposited under ATCC Accession No. PTA-10212. In some embodiments, isolated microorganisms of the invention have growth properties substantially identical to those of the microorganism deposited under ATCC Accession No. PTA-10212. In some embodiments, the invention is directed to an isolated microorganism comprising an 18s rRNA comprising the polynucleotide sequence of SEQ ID NO: l or a polynucleotide sequence having at least 94%, 95%, 96%, 97%, 98%, or 99% identity to SEQ ID NO: l . In some embodiments, the invention is directed to an isolated microorganism comprising an 18s rRNA polynucleotide sequence that has at least 94% identity to the 18s rRNA polynucleotide sequence of the microorganism deposited under ATCC Accession No. PTA- 10212.
[0039] In some embodiments, the invention is directed to a mutant strain of the microorganism deposited under ATCC Accession No. PTA- 10212. In further embodiments, the mutant strain is a strain deposited under ATCC Accession No. PTA- 10213, PTA-10214, or PTA-10215. The microorganisms associated with ATCC Accession Nos. PTA-10213, PTA-10214, and PTA-10215 were deposited under the Budapest Treaty on July 14, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 201 10-2209.
[0040] In some embodiments, the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA-10208. The isolated microorganism associated with ATCC Accession No. PTA-10208 is also known herein as Schizochytrium sp. ATCC PTA-10208. The microorganism associated with ATCC Accession No. PTA-10208 was deposited under the Budapest Treaty on July 14, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 20110-2209. In some embodiments, the invention is directed to an isolated strain deposited under ATCC Accession No. PTA-10208.
[0041] In some embodiments, the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA-10208, wherein the total fatty acids produced by the microorganism comprises more than about 10%, more than about 11%, more than about 12%, more than about 13%, more than about 14%, more than about 15%, more than about 16%, more than about 17%, more than about 18%, more than about 19%, or more than about 20% by weight EPA. In some embodiments, the invention is directed to an isolated microorganism of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises about 10% to about 55%, about 10% to about 50%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, about 20% to about 55%, about 20% to about 50%, about 20% to about 45%, about 20% to about 40%, about 20% to about 35%, or about 20% to about 30%o by weight EPA.
[0042] In some embodiments, the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10%) by weight eicosapentaenoic acid. The characteristics of the microorganism deposited under ATCC Accession No. PTA- 10208 include its growth and phenotypic properties (examples of phenotypic properties include morphological and reproductive properties), its physical and chemical properties (such as dry weights and lipid profiles), its gene sequences, and combinations thereof, in which the characteristics distinguish the species over previously identified species. In some embodiments, the invention is directed to an isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10212, wherein the characteristics include an 18s rRNA comprising the polynucleotide sequence of SEQ ID NO:2, the morphological and reproductive properties of the species deposited under ATCC Accession No. PTA- 10208, and the fatty acid profiles of the species deposited under ATCC Accession No. PTA- 10208. In some embodiments, isolated microorganisms of the invention have physical and chemical properties substantially identical to those of the microorganism deposited under ATCC Accession No. PTA-10208.
[0043] In some embodiments, the invention is directed to a mutant strain of the microorganism deposited under ATCC Accession No. PTA-10208. In further embodiments, the mutant strain is a strain deposited under ATCC Accession No. PTA- 10209, PTA-10210, or PTA-1021 1. The microorganisms associated with ATCC Accession Nos. PTA-10209, PTA-10210, and PTA-1021 1 were deposited under the Budapest Treaty on September 25, 2009 at the American Type Culture Collection, Patent Depository, 10801 University Boulevard, Manassas, VA 20110-2209.
[0044] In some embodiments, the invention is directed to an isolated microorganism of the invention that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight. In some embodiments, the invention is directed to an isolated microorganism that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is about 12% to about 55%, about 12 % to about 50%, about 12% to about 45%, about 12% to about 40%, about 12% to about 35%, about 12% to about 30%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, or about 20%o to about 30% by weight.
In some embodiments, the invention is directed to a mutant, variant, or recombinant of an isolated microorganism of the invention that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is at least about 10%, at least about 1 1%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight. In some embodiments, the invention is directed to a mutant, variant, or recombinant of an isolated microorganism of the invention that produces a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is about 12% to about 55%, about 12% to about 50%, about 12% to about 45%, about 12% to about 40%, about 12% to about 35%, about 12% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, about 20% to about 55%, about 20% to about 50%, about 20% to about 45%, about 20% to about 40%, about 20% to about 35%, or about 20% to about 30% by weight. Mutant strains can be produced by well-known procedures. Common procedures include irradiation, treatment at high temperatures, and treatment with a mutagen. Variant strains can be other naturally occurring isolates and/or sub-isolates of the species described herein. Recombinant strains can be produced by any well-known methods in molecular biology for the expression of exogenous genes or alteration of endogenous gene function or expression. In some embodiments, the mutant, variant, or recombinant strain produces a higher amount of omega-3 fatty acids, particularly EPA, than the wild-type strain. In some embodiments, the mutant, variant, or recombinant strain produces a lower amount of one or more fatty acids, such as lower amounts of DHA, ARA, DPA n-6, or combinations thereof. In some embodiments, the mutant, variant, or recombinant strain produces a larger dry cell weight per liter of culture than the wild-type strain. Such mutant, variant, or recombinant strains are examples of strains derived from an isolated microorganism of the invention. [0046] In some embodiments, an isolated microorganism of the invention, including mutants, variants, and recombinants thereof, comprises a fatty acid profile in one or more fractions isolated from the microorganism. The one or more fractions isolated from the microorganism include the total fatty acid fraction, the sterol esters fraction, the triacylglycerol fraction, the free fatty acid fraction, the sterol fraction, the diacylglycerol fraction, the polar fraction (including the phospholipid fraction), and combinations thereof. The fatty acid profile for a specific fraction can include any of the fatty acid profiles associated with the specific fraction as disclosed herein.
[0047] The invention is directed to a method of producing a mutant comprising mutagenizing any of the microorganisms of the invention and isolating the mutant strain.
Cultures and Isolated Biomasses
[0048] The invention is directed to a culture comprising one or more isolated microorganisms of the invention. Various fermentation parameters for inoculating, growing, and recovering microflora, such as microalgae and thraustochytrids, are known in the art. See, e.g., U.S. Patent No. 5,130,242, incorporated by reference herein in its entirety. Liquid or solid media can contain natural or artificial sea water. Carbon sources for heterotrophic growth include, but are not limited to, glucose, fructose, xylose, saccharose, maltose, soluble starch, molasses, fucose, glucosamine, dextran, fats, oils, glycerol, sodium acetate, and mannitol. Nitrogen sources include, but are not limited to, peptone, yeast extract, polypeptone, malt extract, meat extract, casamino acid, corn steep liquor, organic nitrogen sources, sodium glutamate, urea, inorganic nitrogen sources, ammonium acetate, ammonium sulfate, ammonium chloride, and ammonium nitrate.
[0049] A typical media for growth of the microorganism deposited under ATCC
Accession No. PTA-10212 is shown in Table 1 :
Table 1 : PTA-10212 Vessel Media
Ingredient concentration ranges
Na2S04 g/L 31.0 0-50, 15-45, or 25-35
NaCl g/L 0.625 0-25, 0.1-10, or 0.5-5
KC1 g/L 1.0 0-5, 0.25-3, or 0.5-2
MgS04-7H20 g/L 5.0 0-10, 2-8, or 3-6
(NH4)2S04 g L 0.44 0-10, 0.25-5, or 0.05-3
MSG- 1H20 g/L 6.0 0-10, 4-8, 01- 5-7 CaCl2 g/L 0.29 0.1-5, 0.15-3, or 0.2-1
T 154 (yeast extract) g/L 6.0 0-20, 0.1-10, or 1-7
KH2P04 g/L 0.8 0.1-10, 0.5-5, or 0.6-1.8
Post autoclave (Metals)
Citric acid mg/L 3.5 0.1-5000, 10-3000, or 3-2500
FeS04-7H20 mg/L 10.30 0.1-100, 1-50, or 5-25
MnCl2-4H20 mg/L 3.10 0.1-100, 1-50, or 2-25
ZnS04-7H20 mg/L 3.10 0.01-100, 1-50, or 2-25
CoCl2-6H20 mg/L 0.04 0-1, 0.001-0.1, or 0.01-0.1
Na2Mo04-2H20 mg/L 0.04 0.001-1 , 0.005-0.5, or 0.01-0.1
CuS04'5H20 mg/L 2.07 0.1-100, 0.5-50, or 1 -25
NiS04-6H20 mg/L 2.07 0.1-100, 0.5-50, or 1-25
Post autoclave (Vitamins)
Thiamine mg/L 9.75 0.1-100, 1-50, or 5-25
Vitamin B 12 mg/L 0.16 0.01-100, 0.05-5, or 0.1-1
Ca½-pantothenate mg/L 2.06 0.1-100, 0.1-50, or 1-10
Biotin mg/L 3.21 0.1- 100, 0.1-50, or 1 -10
Post autoclave (Carbon)
Glycerol g/L 30.0 5-150, 10-100, or 20-50
Nitrogen Feed:
Ingredient Concentration
MSG- 1H20 g/L 17 0-150, 10-100, or 15-50
Typical cultivation conditions would include the following: pH about 6.5 - about 9.5, about 6.5 - about 8.0, or about 6.8 - about 7.8;
temperature: about 15 - about 30 degrees Celsius, about 18 - about 28 degrees Celsius, or about 21 to about 23 degrees Celsius; dissolved oxygen: about 0.1 - about 100% saturation, about 5 - about 50% saturation, or about 10 - about 30% saturation; and/or glycerol controlled @: about 5 - about 50 g/L, about 10 - about 40 g/L, or about
15 - about 35 g/L.
[0050] In some embodiments, the microorganism deposited under ATCC Accession No.
PTA-10212, or a mutant, variant, or recombinant thereof, grows heterotrophically on glycerol as the carbon source but does not grow on glucose as the carbon source.
[0051 ] A typical media for growth of the microorganism deposited under ATCC
Accession No. PTA-10208 is shown in Table 2: Table 2: PTA- 10208 Vessel Media
Ingredient concentration ranges
Na2S04 g/L 8.8 0-25, 2-20, or 3-10
NaCl g/L 0.625 0-25, 0.1-10, or 0.5-5
KC1 g/L 1.0 0-5, 0.25-3, or 0.5-2
MgS04-7H20 g/L 5.0 0-10, 2-8, or 3-6
(NH4)2S04 g/L 0.42 0-10, 0.25-5, or 0.05-3
CaCl2 g/L 0.29 0.1-5, 0.15-3, or 0.2-1
T 154 (yeast extract) g/L 1.0 0-20, 0.1-10, or 0.5-5
KH2P04 g/L 1.765 0.1-10, 0.5-5, or 1-3
Post autoclave (Metals)
Citric acid mg/L 46.82 0.1-5000, 10-3000, or 40-2500
FeS04-7H20 mg/L 10.30 0.1-100, 1-50, or 5-25
MnCl2-4H20 mg/L 3.10 0.1-100, 1-50, or 2-25
ZnS04-7H20 mg/L 9.3 0.01 -100, 1 -50, or 2-25
CoCl2-6H20 mg/L 0.04 0-1 , 0.001 -0.1 , or 0.01 -0.1
Na2Mo04-2H20 mg/L 0.04 0.001-1 , 0.005-0.5, or 0.01 -0.1
CuS04-5H20 mg/L 2.07 0.1-100, 0.5-50, or 1-25
NiS04'6H20 mg/L 2.07 0.1- 100, 0.5-50, or 1-25
Post autoclave (Vitamins)
Thiamine mg/L 9.75 0.1-100, 1-50, or 5-25
Ca½-pantothenate mg/L 3.33 0.1-100, 0.1-50, or 1-10
Biotin mg/L 3.58 0.1-100, 0.1-50, or 1-10
Post autoclave (Carbon)
Glucose g/L 30.0 5-150, 10-100, or 20-50
Nitro en Feed:
Ingredient Concentration
NH4OH mL/L 23.6 0-150, 10-100, or 15-50
Typical cultivation conditions would include the following: pH about 6.5 - about 8.5, about 6.5 - about 8.0, or about 7.0 - about 8.0;
temperature: about 17 - about 30 degrees Celsius, about 20 - about 28 degrees Celsius, or about 22 to about 24 degrees Celsius; dissolved oxygen: about 2 - about 100% saturation, about 5 - about 50% saturation, or about 7 - about 20% saturation; and/or glucose controlled about 5 - about 50 g/L, about 10 - about 40 g/L, or about 20 - about 35 g/L. [00521 In some embodiments, the culture medium comprises at least about 0.1%, at least about 0.5%, at least about 1%, at least about 1.5%, at least about 2%, at least about 5%, at least about 7%, at least about 10%, at least about 20%, at least about 30%, at least about 40%, at least about 50%, at least about 60%, at least about 70%, at least about 80%, or at least about 90% dissolved oxygen, as a percentage of saturation level. In some embodiments, the culture medium comprises about 0.1 % to about 2%, about 0.1 % to about 5%, about 0.1 % to about 10%, about 0.1% to about 20%, about 0.1 % to about 30%, about 0.1 % to about 50%, about 0.1% to about 100%, about 5% to about 10%, about 5% to about 20%, about 5% to about 30%, about 5% to about 50%, about 5% to about 100%, about 7% to about 10%, about 7% to about 20%, about 7% to about 30%, about 7% to about 50%, about 7% to about 100%, about 10% to about 20%, about 10% to about 30%, about 10% to about 50%, about 10% to about 100%, about 20% to about 30%, about 20% to about 50%, or about 20% to about 100% dissolved oxygen, as a percentage of saturation level.
[0053] The invention is directed to an isolated biomass of a microorganism of the invention. An isolated biomass of the invention is a harvested cellular biomass obtained by any conventional method for the isolation of a biomass, such as described in U.S. Patent No. 5, 130,242 and U.S. Appl. Publ. No. 2002/0001833, each of which are incorporated by reference herein in its entirety.
[0054] In some embodiments, the dry cell weight of the biomass isolated from each liter of culture is at least about 10 g, at least about 15 g, at least about 20 g, at least about 25 g, at least about 30 g, at least about 50 g, at least about 60 g, at least about 70 g, at least about 80 g, at least about 100 g, at least about 120 g, at least about 140 g, at least about 160 g, at least about 180 g, or at least about 200 g after growing for about 6 days to about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. In some embodiments, the dry cell weight of the biomass isolated from each liter of culture is at least about 10 g, at least about 15 g, at least about 20 g, at least about 25 g, at least about 30 g, at least about 50 g, at least about 60 g, at least about 70 g, at least about 80 g, at least about 100 g, at least about 120 g, at least about 140 g, at least about 160 g, at least about 180 g, or at least about 200 g after growing for about 6 days, about 7 days, or about 8 days at about 15°C, about 16°C, about 17°C, at about 1 8°C, at about 19°C, at about 20°C, at about 21 °C, at about 22°C, at about 23°C, at about 24°C, at about 25°C, at about 26°C, at about 27°C, at about 28°C, at about 29°C, or at about 30°C in a culture medium of about pH 6.5, about pH 7, about pH 7.5, about pH 8.0, about pH 8.5, about pH 9, or about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. In some embodiments, the dry cell weight of the biomass isolated from each liter of culture is about 10 g to about 200 g after growing for about 6 days to about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. hi some embodiments, the dry cell weight of the biomass isolated from each liter of culture is about 10 g to about 200 g, about 10 g to about 100 g, about 10 g to about 50 g, about 15 g to about 200 g, about 15 g to about 100 g, about 15 g to about 50 g, about 20 g to about 200 g, about 20 g to about 100 g, about 20 g to about 50 g, about 50 g to about 200 g, or about 50 g to about 100 g after growing for about 6 days, about 7 days, or about 8 days at about 15°C, about 16°C, about 17°C, at about 18°C, at about 19°C, at about 20°C, at about 21°C, at about 22°C, at about 23°C, at about 24°C, at about 25°C, at about 26°C, at about 27°C, at about 28°C, at about 29°C, or at about 30°C in a culture medium of about pH 6.5, about pH 7, about pH 7.5, about pH 8.0, about pH 8.5, about pH 9, or about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. In some embodiments, the isolated culture does not contain polyvinylpyrrolidone.
In some embodiments, the isolated culture has an omega- 3 fatty acid productivity of at least about 0.2 g/L/day, at least about 0.3 g/L/day, at least about 0.4 g/L/day, at least about 0.5 g/L/day, at least about 1 g/L/day, at least about 1.2 g/L/day, at least about 1.5 g/L/day, at least about 1.7 g/L/day, at least about 2 g/L/day, at least about 3 g/L/day, at least about 3.5 g/L/day, at least about 4 g/L/day, at least about 4.5 g/L/day, at least about 5 g/L/day, at least about 6 g/L/day, or at least about 8 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 8.5 or about pH 6.5 to about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. In some embodiments, the isolated culture has an omega-3 fatty acid productivity of about 0.2 g/L/day to about 20 g/L/day, about 0.4 g/L/day to about 20 g/L/day, about 0.4 g/L/day to about 2 g/L/day, about 1 g/L/day to about 2 g/L/day, about 1 g/L/day to about 20 g/L/day, about 2 g/L/day to about 15 g/L/day, about 2 g/L/day to about 10 g/L/day, about 3 g/L/day to about 10 g/L/day, about 4 g/L/day to about 9 g/L/day, about 4 g/L/day to about 8 g/L/day, about 4 g/L/day to about 7 g/L/day, or about 4 g/L/day to about 6 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions.
In some embodiments, the isolated culture comprises an EPA productivity of at least about 0.2 g/L/day, at least about 0.3 g/L/day, at least about 0.4 g/L/day, at least about 0.5 g/L/day, at least about 0.6 g/L/day, at least about 0.7 g/L/day, at least about 0.8 g/L/day, at least about 0.9 g/L/day, at least about 1 g/L/day, at least about 1.2 g/L/day, at least about 1.5 g/L/day, at least about 1.7 g/L/day, at least about 2 g/L/day, at least about 3 g/L/day, at least about 4 g/L/day, or at least about 5 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 8.5 or about pH 6.5 to about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. In some embodiments, the EPA productivity is about 0.2 g/L/day to about 5 g/L/day, about 0.2 g/L/day to about 4 g/L/day, about 0.2 g/L/day to about 3 g/L/day, about 0.2 g/L/day to about 2 g/L/day, about 0.2 g/L/day to about 1 g/L/day, about 0.2 g/L/day to about 0.8 g/L/day, about 0.2 g/L/day to about 0.7 g/L/day, about 1 g/L/day to about 5 g/L/day, about 1 g/L/day to about 4 g/L/day, about 1 g/L/day to about 3 g/L/day, or about 1 g/L/day to about 2 g/L/day after growing for about 6 days, about 7 days, or about 8 days at about 15°C to about 30°C in a culture medium of about pH 6.5 to about pH 8.5 or about pH 6.5 to about pH 9.5 comprising sources of carbon, nitrogen, and nutrients, and about 950 ppm to about 8500 ppm chloride ions. In some embodiments, any of the aforementioned EPA productivities are associated with any of the aforementioned omega- 3 fatty acid productivities. In some embodiments, the culture further comprises a DHA productivity of about 0 g/L/day to about 5 g/L/day, about 0 g/L/day to about 4 g/L/day, about 0 g/L/day to about 3 g/L/day, about 0 g/L/day to about 2 g/L/day, about 0 g/L/day to about 1 g/L/day, about 0.2 g/L/day to about 5 g/L/day, about 0.2 g/L/day to about 4 g/L/day, about 0.2 g/L/day to about 3 g/L/day, about 0.2 g/L/day to about 2 g/L/day, about 0.2 g/L/day to about 1 g/L/day, about 1 g/L/day to about 5 g/L/day, about 2 g/L/day to about 5 g/L/day, about 2 g/L/day to about 4 g/L/day, or about 2 g/L/day to about 3 g/L/day. In some embodiments, the DHA productivity is less than about 5 g/L/day, less than about 4 g/L/day, less than about 3 g/L/day, less than about 2 g/L/day, less than about 1 g/L/day, less than about 0.5 g/L/day, less than about 0.2 g/L/day, or about 0 g/L/day.
[0057] In some embodiments, the fermentation volume (volume of culture) is at least about 2 liters, at least about 10 liters, at least about 50 liters, at least about 100 liters, at least about 200 liters, at least about 500 liters, at least about 1000 liters, at least about 10,000 liters, at least about 20,000 liters, at least about 50,000 liters, at least about 100,000 liters, at least about 150,000 liters, at least about 200,000 liters, or at least about 250,000 liters. In some embodiments, the fermentation volume is about 2 liters to about 300,000 liters, about 2 liters, about 10 liters, about 50 liters, about 100 liters, about 200 liters, about 500 liters, about 1000 liters, about 10,000 liters, about 20,000 liters, about 50,000 liters, about 100,000 liters, about 150,000 liters, about 200,000 liters, about 250,000 liters, or about 300,000 liters.
[0058] In some embodiments, the invention is directed to an isolated biomass comprising a fatty acid profile of the invention. In some embodiments, at least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%, at least about 45%, at least about 50%, at least about 55%, at least about 60%, at least about 65%, at least about 70%), at least about 75%, or at least about 80% of the dry cell weight of the biomass are fatty acids. In some embodiments, greater than about 20%, greater than about 25%, greater than about 30%, greater than about 35%, greater than about 40%, greater than about 45%, greater than about 50%, greater than about 55%, or greater than about 60% of the dry cell weight of the biomass are fatty acids. In some embodiments, about 20% to about 55%, about 20% to about 60%, about 20% to about 70%, about 20% to about 80%, about 30% to about 55%, about 30% to about 70%, about 30% to about 80%, about 40% to about 60%, about 40% to about 70%, about 40% to about 80%, about 50% to about 60%, about 50% to about 70%, about 50% to about 80%, about 55% to about 70%, about 55% to about 80%, about 60% to about 70%, or about 60% to about 80% by weight of the dry cell weight of the biomass are fatty acids. In some embodiments, the biomass comprises more than about 10%, at least about 12%, at least about 15%, at least about 20%, at least about 25%, at least about 30%, about least about 35%, at least about 40%, or at least about 45% by weight of the fatty acids as EPA. In some embodiments, the biomass comprises about 10% to about 55%, about 12% to about 55%, about 15% to about 55%, about 20% to about 55%, about 20% to about 40%, or about 20% to about 30% by weight of the fatty acids as EPA. In some embodiments, the biomass comprises a triacylglycerol fraction, wherein at least about 12%, at least about 13%, at least about 14%), at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight of the triacylglycerol fraction is EPA. In some embodiments, the biomass comprises a triacylglycerol fraction, wherein the EPA content of the triacylglycerol fraction is from at least about 12% to about 55%, about 12% to about 50%, about 12% to about 45%, at least about 12% to about 40%, at least about 12% to about 35%, or at least about 12% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%, about 15% to about 40%, about 15% to about 35%, about 15% to about 30%, about 20% to about 55%, about 20% to about 50%, about 20% to about 45%, at least about 20% to about 40%o, at least about 20% to about 35%, or about 20% to about 30% by weight. In some embodiments, at least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%, at least about 50%, or at least about 60% by weight of the dry cell weight of the biomass is DHA. In some embodiments, about 20% to about 60%, about 25%o to about 60%, about 25% to about 50%), about 25% to about 45%, about 30% to about 50%, or about 35% to about 50% by weight of the dry cell weight of the biomass is DHA. In some embodiments, the biomass comprises about 10% or less, about 9% or less, about 8% or less, about 7% or less, about 6% or less, about 5% or less, about 4% or less, about 3% or less, about 2% or less, or about 1% or less by weight of the fatty acids as DHA. In some embodiments, the biomass comprises about 1% to about 10%, about 1% to about 5%, about 2% to about 5%, about 3% to about 5%, or about 3% to about 10% by weight of the fatty acids as DHA. In some embodiments, the biomass is substantially free of DHA. In some embodiments, the biomass comprises about 0.1% to less than about 5%, about 0.1% to about 4%, about 0.1% to about 3%, about 0.1% to about 2%, about 0.2% to less than about 5%, about 0.2% to about 4%, about 0.2% to about 3%, about 0.2% to about 2%, about 0.3% to about 2%, about 0.1% to about 0.5%, about 0.2%> to about 0.5%, about 0.1% to about 0.4%, about 0.2% to about 0.4%, about 0.5% to about 2%, about 1% to about 2%, about 0.5%o to about 1.5%>, or about 1%> to about 1.5%> by weight of the fatty acids as ARA. In some embodiments, the biomass comprises less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1.5% or less, about 1% or less, about 0.5% or less, about 0.4% or less, about 0.3% or less, about 0.2% or less, or about 0.1% or less by weight of the fatty acids as ARA. In some embodiments, the biomass is substantially free of ARA. In some embodiments, the biomass comprises about 0.4% to about 2%, about 0.4% to about 3%, about 0.4% to about 4%, about 0.4% to about 5%, about 0.4% to less than about 5%, about 0.5% to about 1%, about 0.5% to about 2%, about 0.5% to about 3%, about 0.5% to about 4%, about 0.5% to about 5%, about 0.5% to less than about 5%, about 1% to about 2%, about 1% to about 3%, about 1% to about 4%, about 1% to about 5%, or about 1% to less than about 5% by weight of the fatty acids as DPA n-6. In some embodiments, the biomass comprises about 5% or less, less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.75% or less, about 0.6% or less, or about 0.5% or less by weight of the fatty acids as DPA n-6. In some embodiments, the biomass is substantially free of DPA n-6. In some embodiments, the biomass comprises fatty acids with about 5% or less, less than about 5%, about 4% or less, about 3% or less, or about 2% or less by weight of oleic acid (18: 1 n-9), linoleic acid (18:2 n-6), linolenic acid (18:3 n-3), eicosenoic acid (20: 1 n-9), erucic acid (22: 1 n-9), or combinations thereof.
[0059] The characteristics of an isolated biomass of the invention are associated with endogenous or native properties of the isolated biomass rather than exogenously introduced materials. In some embodiments, the isolated biomass does not contain polyvinylpyrrolidone or is not isolated from a culture containing polyvinylpyrrolidone.
[0060] The present invention is directed to a method of producing a biomass. In some embodiments, the method for producing a biomass of the invention comprises growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce a biomass. The present invention is directed to a biomass produced by the method.
Microbial Oils
[0061 ] The invention is directed to a microbial oil comprising a fatty acid profile of the invention. A microbial oil of the invention is a "crude oil" or a "refined oil" comprising a triacylglycerol fraction of at least about 35% by weight. A "crude oil" is an oil that is extracted from the biomass of the microorganism without further processing. A "refined oil" is an oil that is obtained by treating a crude oil with standard processing of refining, bleaching, and/or deodorizing. See, e.g., U.S. Patent No. 5,130,242, incorporated by reference herein in its entirety. A microbial oil also includes a "final oil" as described herein, which is a refined oil that has been diluted with a vegetable oil. In some embodiments, a final oil is a refined oil that has been diluted with high oleic sunflower oil. The term "microbial" as used herein includes, but is not limited to, the terms "microalgal," "thraustochytrid," and taxonomic classifications associated with any of the deposited microorganisms described herein. The terms "Thraustochytriales," "thraustochytrid," "Schizochytrium," and "Thranstochytrium" as used in reference to any of the microbial oils of the deposited microorganisms described herein are based on present taxonomic classifications including available phylogenetic information and are not intended to be limiting in the event that the taxonomic classifications are revised after the filing date of the present application.
In some embodiments, a fatty acid as described herein can be a fatty acid ester. In some embodiments, a fatty acid ester includes an ester of an omega-3 fatty acid, omega-6 fatty acid, and combinations thereof. In some embodiments, the fatty acid ester is a DHA ester, an EPA ester, or a combination thereof. In some embodiments, an oil or fraction thereof as described herein is esterified to produce an oil or fraction thereof comprising fatty acid esters. The term "ester" refers to the replacement of the hydrogen in the carboxylic acid group of the fatty acid molecule with another substituent. Typical esters are known to those in the art, a discussion of which is provided by Higuchi, T. and V. Stella in Pro-drugs as Novel Delivery Systems, Vol. 14, A.C.S. Symposium Series, Bioreversible Carriers in Drug Design, Ed. Edward B. Roche, American Pharmaceutical Association, Pergamon Press, 1987, and Protective Groups in Organic Chemistry, McOmie ed., Plenum Press, New York, 1973. Examples of esters include methyl, ethyl, propyl, butyl, pentyl, t-butyl, benzyl, nitrobenzyl, methoxybenzyl, benzhydryl, and trichloroethyl. In some embodiments, the ester is a carboxylic acid protective ester group, esters with aralkyl (e.g., benzyl, phenethyl), esters with lower alkenyl (e.g., allyl, 2- butenyl), esters with lower-alkoxy-lower-alkyl (e.g., methoxymethyl, 2-methoxyethyl, 2- ethoxyethyl), esters with lower- alkanoyloxy- lower- alkyl (e.g., acetoxymethyl, pivaloyloxymethyl, 1-pivaloyloxyethyl), esters with lower-alkoxycarbonyl-lower-alkyl (e.g., methoxycarbonylmethyl, isopropoxycarbonylmethyl), esters with carboxy-lower alkyl (e.g., carboxymethyl), esters with lower-alkoxycarbonyloxy-lower-alkyl (e.g., 1- (ethoxycarbonyloxy)ethyl, l-(cyclohexyloxycarbonyloxy)ethyl), esters with carbamoyloxy-lower alkyl (e.g., carbamoyloxymethyl), and the like. In some embodiments, the added substituent is a linear or cyclic hydrocarbon group, e.g., a C1-C6 alkyl, C1-C6 cycloalkyl, C1-C6 alkenyl, or C1-C6 aryl ester. In some embodiments, the ester is an alkyl ester, e.g., a methyl ester, ethyl ester or propyl ester. In some embodiments, the ester substituent is added to the free fatty acid molecule when the fatty acid is in a purified or semi-purified state. Alternatively, the fatty acid ester is formed upon conversion of a triacylglycerol to an ester.
[0063] The present invention is directed to methods of producing microbial oils. In some embodiments, the method comprises growing any of the isolated microorganisms of the invention or mixtures thereof in a culture to produce a microbial oil comprising omega-3 fatty acids. In some embodiments, the method further comprises extracting the microbial oil. In some embodiments, the method comprises extracting a microbial oil comprising omega-3 fatty acids from any of the biomasses of the invention or mixtures thereof. In some embodiments, the method comprises heterotrophically growing the isolated microorganism, wherein the culture comprises a carbon source as described herein. The microbial oil can be extracted from a freshly harvested biomass or can be extracted from a previously harvested biomass that has been stored under conditions that prevent spoilage. Known methods can be used to culture a microorganism of the invention, to isolate a biomass from the culture, to extract a microbial oil from the biomass, and to analyze the fatty acid profile of oils extracted from the biomass. See, e.g., U.S. Patent No. 5,130,242, incorporated by reference herein in its entirety. The invention is directed to a microbial oil produced by any of the methods of the invention.
[0064] In some embodiments, the microbial oil is extracted by an enzyme extraction method. In some embodiments, the microbial oil is extracted by a mechanical extraction method. In some embodiments, the mechanical extraction method comprises one or more of: (1) processing a pasteurized fermentation broth through a homogenizer to assist in cell lysis and release of oil from cells; (2) adding isopropyl alcohol to the fermentation broth following homogenization to break the oil and water emulsion; (3) centrifuging the mixture to recover the oil phase; and (4) drying under vacuum with addition of antioxidants. In some embodiments, the crude oil is purified. In some embodiments, purification of the crude oil comprises one or more of: (1) pumping the crude oil into a refining tank and heating the oil, followed by adding an acid solution with mixing; (2) adding a caustic solution to the oil after acid treatment; (3) reheating the crude oil and then centrifuging to separate the heavy phase from the refined oil; (4) removing the remaining polar compounds, trace metals, and oxidation products from the refined oil by using, for example, acid, TriSyl®, clay, and/or filtration; (5) chill filtering the bleached oil to further remove high melting point components from the oil to achieve the desired level of clarity; (6) heating the oil, after which the oil is then cooled and held for a period of time causing the high melting triglycerides and waxes to crystallize; (7) adding a filter aid to the chilled oil and then removing crystallized solids by filtration; (8) using a deodorizer after chill filtration, operated under high temperature and vacuum, to remove, for example, peroxides and any remaining low molecular weight compounds that can cause off-odor and flavors; (9) transferring the oil to the deodorizer feed tank, deaerating, and deodorizing, for example, in a packed column deodorizer; and (10) cooling, for example, under a nitrogen blanket at the end of the deodorization cycle and adding suitable antioxidants to the deodorized oil to provide oxidative stability.
[00651 In some embodiments, the microbial oil comprises a sterol esters fraction of about
0%, at least about 0.1 %, at least about 0.2%, at least about 0.5%, at least about 1 %, at least about 1.5%, at least about 2%, or at least about 5% by weight. In some embodiments, the microbial oil comprises a sterol esters fraction of about 0% to about 1.5%, about 0% to about 2%, about 0% to about 5%, about 1% to about 1.5%, about 0.2% to about 1.5%, about 0.2% to about 2%, or about 0.2%> to about 5% by weight. In some embodiments, the microbial oil comprises a sterol esters fraction of about 5% or less, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.5% or less, about 0.3% or less, about 0.2%0 or less, about 0.5% or less, about 0.4% or less, about 0.3% or less, or about 0.2% or less by weight.
[0066] In some embodiments, the microbial oil comprises a triacylglycerol fraction of at least about 35%, at least about 40%, at least about 45%, at least about 50%, at least about 55%, at least about 60%, at least about 65%, at least about 70%>, at least about 75%, at least about 80%, at least about 85%, or at least about 90% by weight. In some embodiments, the microbial oil comprises a triacylglycerol fraction of about 35% to about 98%, about 35% to about 90%, about 35% to about 80%, about 35% to about 70%, about 35% to about 70%, about 35% to about 65%, about 40% to about 70%, about 40% to about 65%, about 40% to about 55%, about 40% to about 50%, about 65% to about 95%, about 75% to about 95%, about 75% to about 98%, about 80% to about 95%, about 80% to about 98%, about 90% to about 96%, about 90% to about 97%, about 90% to about 98%, about 90%, about 95%, about 97%, or about 98% by weight.
In some embodiments, the microbial oil comprises a diacylglycerol fraction of at least about 10%, at least about 1 1%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight. In some embodiments, the microbial oil comprises a diacylglycerol fraction of about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 15% to about 40%, about 15% to about 35%, or about 15% to about 30% by weight. In some embodiments, the microbial oil comprises a 1 ,2-diacylglycerol fraction of at least about 0.2%, at least about 0.3%, at least about 0.4%, at least about 0.5%, at least about 1%, at least about 5%, at least about 10%, at least about 11%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, or at least about 20% by weight. In some embodiments, the microbial oil comprises a diacylglycerol fraction of about 0.2%> to about 45%, about 0.2% to about 30%, about 0.2% to about 20%, about 0.2% to about 10%, about 0.2% to about 5%, about 0.2% to about 1%, about 0.2% to about 0.8%, about 0.4% to about 45%, about 0.4% to about 30%, about 0.4% to about 20%, about 0.4% to about 10%, about 0.4% to about 5%, about 0.4% to about 1%, about 0.4% to about 0.8%, about 0.5% to about 1%, about 0.5% to about 0.8%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 15% to about 40%, about 15% to about 35%, about 15%) to about 30%), or about 15% to about 25% by weight. In some embodiments, the microbial oil comprises a 1,3-diacylglycerol fraction of at least about 0.1%, at least about 0.2%, at least about 0.5%, at least about 1%, at least about 2%, at least about 2.5 %, or at least about 3% by weight. In some embodiments, the microbial oil comprises a sterol fraction of at least about 0.3%, at least about 0.4%, at least about 0.5%, at least about 1%, at least about 1.5%, at least about 2%>, or at least about 5% by weight.
In some embodiments, the microbial oil comprises a sterol fraction of about 0.3% to about 5%, about 0.3% to about 2%, about 0.3% to about 1.5%, about 0.5% to about 1.5%, about 1% to about 1.5%, about 0.5% to about 2%, about 0.5% to about 5%, about 1% to about 2%, or about 1% to about 5% by weight. In some embodiments, the microbial oil comprises a sterol fraction of about 5% or less, about 4% or less, about 3% or less, about 2% or less, about 1.5% or less, or about 1% or less by weight.
In some embodiments, the microbial oil comprises a phospholipid fraction of at least about 2%, at least about 5%, or at least about 8% by weight. In some embodiments, the microbial oil comprises a phospholipid fraction of about 2% to about 25%, about 2% to about 20%, about 2% to about 15%, about 2% to about 10%, about 5% to about 25%, about 5% to about 20%, about 5% to about 20%, about 5% to about 10%, or about 7% to about 9% by weight. In some embodiments, the microbial oil comprises a phospholipid fraction of less than about 20%, less than about 15%, less than about 10%, less than about 9%, or less than about 8% by weight. In some embodiments, the microbial oil is substantially free of phospholipids. In some embodiments, the microbial oil comprises unsaponifiables of less than about 2%, less than about 1.5%, less than about 1%, or less than about 0.5% by weight of the oil. The lipid classes present in the microbial oil, such as a triacylglycerol fraction, can be separated by flash chromatography and analyzed by thin layer chromatography (TLC), or separated and analyzed by other methods known in the art.
In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the free fatty acid fraction, the sterol fraction, the diacylglycerol fraction, and combinations thereof, comprises at least about 5%, at least about 10%, more than about 10%, at least about 12%, at least about 13%, at least about 14%, at least about 15%, at least about 16%, at least about 17%, at least about 18%, at least about 19%, at least about 20%, at least about 25%, at least about 30%, about least about 35%, at least about 40%, or at least about 45%o by weight EPA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the free fatty acid fraction, the sterol fraction, the diacylglycerol fraction, and combinations thereof, comprises about 5% to about 55%, about 5% to about 50%, about 5% to about 45%, about 5% to about 40%, about 5% to about 35%, about 5% to about 30%, about 10% to about 55%, about 10% to about 50%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, at least about 12% to about 55%, at least about 12% to about 50%, at least about 12% to about 45%, at least about 12% to about 40%, at least about 12% to about 35%, or at least about 12% to about 30%, about 15% to about 55%, about 15% to about 50%, about 15% to about 45%), about 15% to about 40%, about 15% to about 35%, about 15% to about 30%), about 15% to about 25%, about 15% to about 20%, about 20% to about 55%o, about 20% to about 50%, about 20% to about 45%, about 20% to about 40%, or about 20% to about 30% by weight EPA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises at least about 5%, at least about 10%, at least about 15%, at least about 20%, at least about 25%, at least about 30%, at least about 35%, at least about 40%o, at least about 50%0, or at least about 60% by weight DHA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 5%> to about 60%, about 5% to about 55%, about 5% to about 50%, about 5% to about 40%, about 10% to about 60%, about 10% to about 50%, about 10% to about 40%, about 20% to about 60%, about 25% to about 60%, about 25% to about 50%, about 25% to about 45%, about 30% to about 50%, about 35% to about 50%, or about 30% to about 40%) by weight DHA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 10% or less, about 9% or less, about 8% or less, about 7% or less, about 6% or less, about 5% or less, about 4% or less, about 3%> or less, about 2%> or less, or about \ % or less by weight DHA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 1 % to about 10%, about 1% to about 5%, about 2% to about 5%, about 3% to about 5%>, or about 3% to about 10% by weight of the fatty acids as DHA. In some embodiments, the microbial oil and/Or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, is substantially free of DHA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 0.1% to about 5%, about 0.1% to less than about 5%, about 0.1% to about 4%, about 0.1% to about 3%, about 0.1% to about 2%, about 0.2%) to about 5%, about 0.2% to less than about 5%, about 0.2% to about 4%, about 0.2% to about 3%, about 0.2% to about 2%, about 0.3% to about 2%, about 0.1% to about 0.5%, about 0.2% to about 0.5%, about 0.1 % to about 0.4%, about 0.2% to about 0.4%, about 0.5% to about 2%, about 1 % to about 2%, about 0.5% to about 1.5%, or about 1% to about 1.5% by weight A A. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 5% or less, less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1.5% or less, about 1% or less, about 0.5% or less, about 0.4% or less, about 0.3%o or less, about 0.2% or less, or about 0.1% or less by weight ARA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, is substantially free of ARA. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 0.4% to about 2%, about 0.4% to about 3%, about 0.4% to about 4%, about 0.4%) to about 5%, about 0.4% to less than about 5%, about 0.5% to about 1%, about 0.5% to about 2%, about 0.5% to about 3%, about 0.5% to about 4%, about 0.5% to about 5%, about 0.5% to less than about 5%, about 1 % to about 2%, about 1 % to about 3%, about 1% to about 4%, about 1% to about 5%, or about 1% to less than about 5% by weight DPA n-6. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises about 5%, less than about 5%, about 4% or less, about 3% or less, about 2% or less, about 1% or less, about 0.75% or less, about 0.6% or less, or about 0.5%) or less by weight DPA n-6. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, is substantially free of DPA n-6. In some embodiments, the microbial oil and/or one or more fractions thereof selected from the triacylglycerol fraction, the diacylglycerol fraction, the sterol fraction, the sterol esters fraction, the free fatty acids fraction, the phospholipid fraction, and combinations thereof, comprises fatty acids with about 5% or less, less than about 5%, about 4% or less, about 3% or less, or about 2% or less by weight of oleic acid (18: 1 n-9), linoleic acid (18:2 n-6), linolenic acid (18:3 n-3), eicosenoic acid (20: 1 n-9), erucic acid (22: 1 n-9), stearidonic acid (18:4 n-3), or combinations thereof.
The triacylglycerol molecule contains 3 central carbon atoms (C(-S7i-l)H2Rl-(s«-
2 ) H 2 R2-C(.s ;-3 ) 1 12 R3 ). allowing for formation of different positional isomers. In some embodiments, the microbial oil comprises a triacylglycerol fraction in which at least about 2%, at least about 3%, at least about 5%, at least about 10%, at least about 15%, at least about 20%>, at least about 30%>, at least about 35%», or at least about 40%> of the triacylglycerols in the triacylglycerol fraction contain DHA at two positions in the triacylglycerol (di-substituted DHA) selected from any two of the sn-l, sn-2, and sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph. In some embodiments, the microbial oil comprises a triacylglycerol fraction in which about 2% to about 55%, about 2% to about 50%, about 2% to about 45%, about 2% to about 40%, about 2% to about 35%, about 2% to about 30%, about 2% to about 25%, about 5% to about 55%, about 5% to about 50%, about 5% to about 45%, about 5% to about 40%, about 5%) to about 35%, about 5% to about 30%, about 5% to about 25%, about 10% to about 55%o, about 10% to about 50%, about 10% to about 45%, about 10% to about 40%, about 10% to about 35%, about 10% to about 30%, about 10% to about 25%, about 10% to about 20%), about 20% to about 40%, about 20%o to about 35%, or about 20% to about 25%o of the triacylglycerols in the triacylglycerol fraction contain EPA at two positions in the triacylglycerol selected from any two of the sn-l, sn-2, or sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph. In some embodiments, the microbial oil comprises a triacylglycerol fraction in which at least about 0.5%, at least about 1%, at least about 1.5%, or at least about 2% of the triacylglycerols in the triacylglycerol fraction contain DHA at all of the sn-l, sn-2, and sn-3 positions (tri- substituted DHA), based on the relative area percent of peaks on an HPLC chromatograph. In some embodiments, the microbial oil comprises a triacylglycerol fraction in which about 0.5% to about 5%, about 0.5% to about 3%, about 0.5% to about 2.5%, about 0.5%o to about 2%, about 1 % to about 5%, about 1 % to about 3%, or about 1 % to about 2%o of the triacylglycerols in the triacylglycerol fraction contain DHA at all of the sn-l, sn-2, and sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph. In some embodiments, the microbial oil comprises a triacylglycerol fraction in which at least about 10%, at least about 15%, at least about 20%, at least about 25%, at least about 30%, at least about 35%o, at least about 40%, at least about 45%, at least about 50%>, at least about 55%, or at least about 60% of the triacylglycerols in the triacylglycerol fraction contain DHA at one position in the triacylglycerol selected from any one of the sn-l, sn-2, or sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph. In some embodiments, the microbial oil comprises a triacylglycerol fraction in which about 10% to about 80%, about 10% to about 70%, about 10% to about 60%, about 15% to about 80%, about 15% to about 75%>, about 15% to about 70%, about 15% to about 65%, about 15% to about 60%, about 35% to about 80%, about 35% to about 75%, about 35% to about 65%, about 35% to about 60%o, about 40% to about 80%, about 40% to about 75%, about 40% to about 70%, about 40% to about 65%, about 40%o to about 60%, or about 40% to about 55% of the triacylglycerols in the triacylglycerol fraction contain DHA at one position in the triacylglycerol selected from any one of the sn-l, sn-2, and sn-3 positions, based on the relative area percent of peaks on an HPLC chromatograph.
Compositions
[0072] The invention is directed to compositions comprising a microorganism of the invention, an isolated biomass of the invention, a microbial oil of the invention, or combinations thereof.
[0073] A microorganism, biomass, or microbial oil of the invention can be further chemically or physically modified or processed based on the requirements of the composition by any known technique.
[0074] Microorganism cells or biomasses can be dried prior to use in a composition by methods including, but not limited to, freeze drying, air drying, spray drying, tunnel drying, vacuum drying (lyophilization), and a similar process. Alternatively, a harvested and washed biomass can be used directly in a composition without drying. See, e.g., U.S. Patent Nos. 5,130,242 and 6,812,009, each of which is incorporated by reference herein in its entirety.
[0075] Microbial oils of the invention can be used as starting material to more efficiently produce a product enriched in a fatty acid such as EPA. For example, the microbial oils of the invention can be subjected to various purification techniques known in the art, such as distillation or urea adduction, to produce a higher potency product with higher concentrations of EPA or another fatty acid. The microbial oils of the invention can also be used in chemical reactions to produce compounds derived from fatty acids in the oils, such as esters and salts of EPA or another fatty acid.
[0076] A composition of the invention can include one or more excipients. As used herein, "excipient" refers to a component, or mixture of components, that is used in a composition of the present invention to give desirable characteristics to the composition, including foods as well as pharmaceutical, cosmetic, and industrial compositions. An excipient of the present invention can be described as a "pharmaceutically acceptable" excipient when added to a pharmaceutical composition, meaning that the excipient is a compound, material, composition, salt, and/or dosage form which is, within the scope of sound medical judgment, suitable for contact with tissues of human beings and non- human animals without excessive toxicity, irritation, allergic response, or other problematic complications over the desired duration of contact commensurate with a reasonable benefit/risk ratio. In some embodiments, the term "pharmaceutically acceptable" means approved by a regulatory agency of the Federal or a state government or listed in the U.S. Pharmacopeia or other generally recognized international pharmacopeia for use in animals, and more particularly in humans. Various excipients can be used. In some embodiments, the excipient can be, but is not limited to, an alkaline agent, a stabilizer, an antioxidant, an adhesion agent, a separating agent, a coating agent, an exterior phase component, a controlled-release component, a solvent, a surfactant, a humectant, a buffering agent, a filler, an emollient, or combinations thereof. Excipients m addition to those discussed herein can include excipients listed in, though not limited to, Remington: The Science and Practice of Pharmacy, 21st ed. (2005). Inclusion of an excipient in a particular classification herein (e.g., "solvent") is intended to illustrate rather than limit the role of the excipient. A particular excipient can fall within multiple classifications.
[0077] Compositions of the invention include, but are not limited to, food products, pharmaceutical compositions, cosmetics, and industrial compositions.
[0078] In some embodiments, the composition is a food product. A food product is any food for non-human animal or human consumption, and includes both solid and liquid compositions. A food product can be an additive to animal or human foods. Foods include, but are not limited to, common foods; liquid products, including milks, beverages, therapeutic drinks, and nutritional drinks; functional foods; supplements; nutraceiiticals; infant formulas, including formulas for pre-mature infants; foods for pregnant or nursing women; foods for adults; geriatric foods; and animal foods.
[0079] In some embodiments, a microorganism, biomass, or microbial oil of the invention can be used directly as or included as an additive within one or more of: an oil, shortening, spread, other fatty ingredient, beverage, sauce, dairy-based or soy-based food (such as milk, yogurt, cheese and ice-cream), a baked good, a nutritional product, e.g., as a nutritional supplement (in capsule or tablet form), a vitamin supplement, a diet supplement, a powdered drink, and a finished or semi-finished powdered food product. In some embodiments, the nutritional supplement is in the form of a vegetarian capsule that is not formed from and does not contain any components from an animal source.
[0080] A partial list of food compositions that can include a microbial oil of the invention includes, but is not limited to, soya based products (milks, ice creams, yogurts, drinks, creams, spreads, whiteners); soups and soup mixes; doughs, batters, and baked food items including, for example, fine bakery wares, breakfast cereals, cakes, cheesecakes, pies, cupcakes, cookies, bars, breads, rolls, biscuits, muffins, pastries, scones, croutons, crackers, sweet goods, snack cakes, pies, granola/snack bars, and toaster pastries; candy; hard confectionery; chocolate and other confectionery; chewing gum; liquid food products, for example milks, energy drinks, infant formula, carbonated drinks, teas, liquid meals, fruit juices, fruit-based drinks, vegetable-based drinks; multivitamin syrups, meal replacers, medicinal foods, and syrups; powdered beverage mixes; pasta; processed fish products; processed meat products; processed poultry products; gravies and sauces; condiments (ketchup, mayonnaise, etc.); vegetable oil-based spreads; dairy products; yogurt; butters; frozen dairy products; ice creams; frozen desserts; frozen yogurts; semi- solid food products such as baby food; puddings and gelatin desserts; processed and unprocessed cheese; pancake mixes; food bars including energy bars; waffle mixes; salad dressings; replacement egg mixes; nut and nut-based spreads; salted snacks such as potato chips and other chips or crisps, corn chips, tortilla chips, extruded snacks, popcorn, pretzels, potato crisps, and nuts; and specialty snacks such as dips, dried fruit snacks, meat snacks, pork rinds, health food bars and rice/corn cakes.
10081 J In some embodiments, a microbial oil of the invention can be used to supplement infant formula. Infant formula can be supplemented with a microbial oil of the invention alone or in combination with a physically refined oil derived from an arachidonic acid (ARA)-producing microorganism. An ARA-producing microorganism, for example, is Mortierella alpina or Mortierella sect, schmuckeri. Alternatively, infant formulas can be supplemented with a microbial oil of the invention in combination with an oil rich in ARA, including ARASCO® (Martek Biosciences, Columbia, MD).
[0082] In some embodiments, the composition is an animal feed. An "animal" includes non-human organisms belonging to the kingdom Animalia, and includes, without limitation, aquatic animals and terrestrial animals. The term "animal feed" or "animal food" refers to any food intended for non-human animals, whether for fish; commercial fish; ornamental fish; fish larvae; bivalves; mollusks; crustaceans; shellfish; shrimp; larval shrimp; artemia; rotifers; brine shrimp; filter feeders; amphibians; reptiles; mammals; domestic animals; farm animals; zoo animals; sport animals; breeding stock; racing animals; show animals; heirloom animals; rare or endangered animals; companion animals; pet animals such as dogs, cats, guinea pigs, rabbits, rats, mice, or horses; primates such as monkeys (e.g., cebus, rhesus, African green, patas, cynomolgus, and cercopithecus), apes, orangutans, baboons, gibbons, and chimpanzees; canids such as dogs and wolves; felids such as cats, lions, and tigers; equids such as horses, donkeys, and zebras; food animals such as cows, cattle, pigs, and sheep; ungulates such as deer and giraffes; or rodents such as mice, rats, hamsters and guinea pigs; and so on. An animal feed includes, but is not limited to, an aquaculture feed, a domestic animal feed including pet feed, a zoological animal feed, a work animal feed, a livestock feed, and combinations thereof.
[0083] In some embodiments, the composition is a feed or feed supplement for any animal whose meat or products are consumed by humans, such as any animal from which meat, eggs, or milk is derived for human consumption. When fed to such animals, nutrients such as LC-PUFAs can be incorporated into the flesh, milk, eggs or other products of such animals to increase their content of these nutrients.
[0084] In some embodiments, the composition is a spray-dried material that can be crumbled to form particles of an appropriate size for consumption by zooplankton, artemia, rotifers, and filter feeders. In some embodiments, the zooplankton, artemia, or rotifers fed by the composition are in turn fed to fish larvae, fish, shellfish, bivalves, or crustaceans.
[0085] In some embodiments, the composition is a pharmaceutical composition. Suitable pharmaceutical compositions include, but are not limited to, an anti-inflammatory composition, a drug for treatment of coronary heart disease, a drug for treatment of arteriosclerosis, a chemotherapeutic agent, an active excipient, an osteoporosis drug, an anti-depressant, an anti-convulsant, an anti-Helicobacter pylori drug, a drug for treatment of neurodegenerative disease, a drug for treatment of degenerative liver disease, an antibiotic, a cholesterol lowering composition, and a triacylglycerol lowering composition. In some embodiments, the composition is a medical food. A medical food includes a food that is in a composition to be consumed or administered externally under the supervision of a physician and that is intended for the specific dietary management of a condition, for which distinctive nutritional requirements, based on recognized scientific principles, are established by medical evaluation.
[0086] In some embodiments, the microbial oil can be formulated in a dosage form.
Dosage forms can include, but are not limited to, tablets, capsules, cachets, pellets, pills, powders and granules, and parenteral dosage forms, which include, but are not limited to, solutions, suspensions, emulsions, and dry powders comprising an effective amount of the microbial oil. It is also known in the art that such formulations can also contain pharmaceutically acceptable diluents, fillers, disintegrants, binders, lubricants, surfactants, hydrophobic vehicles, water soluble vehicles, emulsifiers, buffers, humectants, moisturizers, solubilizers, preservatives and the like. Administration forms can include, but are not limited to, tablets, dragees, capsules, caplets, and pills, which contain the microbial oil and one or more suitable pharmaceutically acceptable carriers.
[0087] For oral administration, the microbial oil can be combined with pharmaceutically acceptable carriers well known in the art. Such carriers enable the microbial oils of the invention to be formulated as tablets, pills, dragees, capsules, liquids, gels, syrups, slurries, suspensions and the like, for oral ingestion by a subject to be treated. In some embodiments, the dosage form is a tablet, pill or caplet. Pharmaceutical preparations for oral use can be obtained by adding a solid excipient, optionally grinding the resulting mixture, and processing the mixture of granules, after adding suitable auxiliaries, if desired, to obtain tablets or dragee cores. Suitable excipients include, but are not limited to, fillers such as sugars, including, but not limited to, lactose, sucrose, mannitol, and sorbitol; cellulose preparations such as, but not limited to, maize starch, wheat starch, rice starch, potato starch, gelatin, gum tragacanth, methyl cellulose, hydroxypropylmethyl cellulose, sodium carboxymethyl cellulose, and polyvinylpyrrolidone (PVP). If desired, disintegrating agents can be added, such as, but not limited to, the cross-linked polyvinylpyrrolidone, agar, or alginic acid or a salt thereof such as sodium alginate. Pharmaceutical preparations that can be used orally include, but are not limited to, push- fit capsules made of gelatin, as well as soft, sealed capsules made of gelatin and a plasticizer, such as glycerol or sorbitol. In some embodiments, the dosage form is a vegetarian dosage form, in which the dosage form is not formed from and does not contain any components from an animal source. In some embodiments, the vegetarian dosage form is a vegetarian capsule.
[0088] In some embodiments, the composition is a cosmetic. Cosmetics include, but are not limited to, emulsions, creams, lotions, masks, soaps, shampoos, washes, facial creams, conditioners, make-ups, bath agents, and dispersion liquids. Cosmetic agents can be medicinal or non-medicinal.
[0089] In some embodiments, the composition is an industrial composition. In some embodiments, the composition is a starting material for one or more manufactures. A manufacture includes, but is not limited to, a polymer; a photographic photosensitive material; a detergent; an industrial oil; or an industrial detergent. For example, U.S. Patent No. 7,259,006 describes use of DHA-containing fat and oil for production of behenic acid and production of photographic sensitive materials using behenic acid.
Methods of Using the Compositions
[0090] In some embodiments, the compositions can be used in the treatment of a condition in humans or non-human animals. In some embodiments, the compositions can be used for nutrition in humans or non-human animals. The terms "treat" and "treatment" refer to both therapeutic treatment and prophylactic or preventative measures, wherein the object is to prevent or slow down (lessen) an undesired physiological condition, disease, or disorder, or to obtain beneficial or desired clinical results. For purposes of this invention, beneficial or desired clinical results include, but are not limited to, alleviation or elimination of the symptoms or signs associated with a condition, disease, or disorder; diminishment of the extent of a condition, disease, or disorder; stabilization of a condition, disease, or disorder, (i.e., where the condition, disease, or disorder is not worsening); delay in onset or progression of the condition, disease, or disorder; amelioration of the condition, disease, or disorder; remission (whether partial or total and whether detectable or undetectable) of the condition, disease, or disorder; or enhancement or improvement of a condition, disease, or disorder. Treatment includes eliciting a clinically significant response without excessive side effects. Treatment also includes prolonging survival as compared to expected survival if not receiving treatment.
In some embodiments, the composition is used to treat a condition, disease, or disorder such as acne, acute inflammation, age related maculopathy, allergy, Alzheimer's, arthritis, asthma, atherosclerosis, autoimmune disease, blood lipid disorder, breast cysts, cachexia, cancer, cardiac restenosis, cardiovascular diseases, chronic inflammation, coronary heart disease, cystic fibrosis, degenerative disorder of the liver, diabetes, eczema, gastrointestinal disorder, heart disease, high triacylglycerol levels, hypertension, hyperactivity, immunological diseases, inhibiting tumor growth, inflammatory conditions, intestinal disorders, kidney dysfunction, leukemia, major depression, multiple sclerosis, neurodegenerative disorder, osteoarthritis, osteoporosis, peroxisomal disorder, preeclampsia, preterm birth, psoriasis, pulmonary disorder rheumatoid arthritis, risk of heart disease, or thrombosis.
[0093] In some embodiments, the composition is used to increase the length of gestation of a fetus in the third trimester.
[0094] In some embodiments, the composition is used to control blood pressure.
[0095] In some embodiments, the composition is used to improve or maintain cognitive function.
[0096] In some embodiments, the composition is used to improve or maintain memory. [0097] The composition or dosage form can be administered into the body of a subject by any route compatible with the composition or dosage form. A substance is considered to be "administered" if the substance is introduced into the body of the subject by the subject, or if another person, a machine, or a device introduces the substance into the body of the subject. "Administering," therefore, includes, e.g., self-administration, administration by others, and indirect administration. The term "continuous" or "consecutive," as used herein in reference to "administration," means that the frequency of administration is at least once daily. Note, however, that the frequency of administration can be greater than once daily and still be "continuous" or "consecutive," e.g., twice or even three times daily, as long as the dosage levels as specified herein are not exceeded. The means and methods for administration are known in the art and an artisan can refer to various pharmacologic references for guidance. For example, "Modern Pharmaceutics," Banker & Rhodes, In forma Healthcare, USA, 4th ed. (2002); and "Goodman & Gilman's The Pharmaceutical Basis of Therapeutics," McGraw-Hill Companies, Inc., New York, 10th ed. (2001) can be consulted.
[0098] By "subject," "individual," or "patient" is meant any subject, whether human or non-human, for whom diagnosis, prognosis, therapy, or administration of the composition or dosage form is desired. Mammalian subjects include, but are not limited to, humans; domestic animals; farm animals; zoo animals; sport animals; pet animals such as dogs, cats, guinea pigs, rabbits, rats, mice, or horses; primates such as monkeys (e.g., cebus, rhesus, African green, patas, cynomolgus, and cercopithecus), apes, orangutans, baboons, gibbons, and chimpanzees; canids such as dogs and wolves; felids such as cats, lions, and tigers; equids such as horses, donkeys, and zebras; food animals such as cows, cattle, pigs, and sheep; ungulates such as deer and giraffes; rodents such as mice, rats, hamsters and guinea pigs; and so on. The term subject also encompasses model animals, e.g., disease model animals. In some embodiments, the term subject includes valuable animals, either economically or otherwise, e.g., economically important breeding stock, racing animals, show animals, heirloom animals, rare or endangered animals, or companion animals. In certain embodiments, the subject is a human subject. In certain embodiments, the subject is a non-human subject.
[0099] The composition can be administered as a "nutritional amount," "therapeutically effective amount," a "prophylactically effective amount," a "therapeutic dose," or a "prophylactic dose." A "nutritional amount" refers to an amount effective, at dosages and for periods of time necessary, to achieve a desired nutritional result. A nutritional result can be, e.g., increased levels of a desirable fatty acid component in a subject. A "therapeutically effective amount" or "therapeutic dose" refers to an amount effective, at dosages and for periods of time necessary, to achieve a desired therapeutic result. A therapeutic result can be, e.g., lessening of symptoms, prolonged survival, improved mobility, and the like. A therapeutic result need not be a "cure." A "prophylactically effective amount" or "prophylactic dose" refers to an amount effective, at dosages and for periods of time necessary, to achieve the desired prophylactic result. Typically, since a prophylactic dose is used in subjects prior to or at an earlier stage of disease, a prophylactically effective amount will be less than a therapeutically effective amount for treatment of an advanced stage of disease.
Various dosage amounts of the composition, dosage form, or pharmaceutical composition can be administered to a subject, based on the amount of EPA or other fatty acid component of the microorganism, biomass, or microbial oil to be administered to the subject. The terms "daily dosage," "daily dosage level," and "daily dosage amount" refer herein to the total amount of EPA or other fatty acid component administered per day (per 24 hour period). Thus, for example, administration of EPA to a subject at a daily dosage of 2 mg means that the subject receives a total of 2 mg of EPA on a daily basis, whether the EPA is administered as a single dosage form comprising 2 mg EPA, or alternatively, four dosage forms comprising 0.5 mg EPA each (for a total of 2 mg EPA). In some embodiments, the daily amount of EPA is administered in a single dosage form, or in two dosage forms. The dosage forms of the present invention can be taken in a single application or multiple applications. For example, if four tablets are taken daily, each tablet comprising 0.5 mg EPA, then all four tablets can be taken once daily, or 2 tablets can be taken twice daily, or 1 tablet can be taken every 6 hours. In some embodiments, the daily dosage is about 100 mg to about 15 g of EPA. In some embodiments, the daily dosage is about 0.5 mg to about 250 mg, about 100 mg to about 250 mg, about 100 mg to about 500 mg, about 100 mg to about 1 g, about 1 g to about 2.5 g, about 1 g to about 5 g, about 1 g to about 10 g, about 1 g to about 15 g, about 5 g to about 10 g, about 5 g to about 15 g, about 10 g to about 15 g, about 100 mg to about 10 g, about 100 mg to about 5 g, or about 100 mg to about 2.5 g of EPA, DHA, or a combination thereof. In some embodiments, the composition is a dosage form that comprises about 0.5 mg to about 250 mg, 100 mg to about 250 mg, about 0.5 mg to about 500 mg, about 100 mg to about 500 mg, about 0.5 mg to about 1 g, or about 100 mg to about 1 g of EPA, DHA, or a combination thereof per dosage form.
[0101] Administration of the compositions or dosage forms of the present invention can be achieved using various regimens. For example, in some embodiments, administration occurs daily on consecutive days, or alternatively, occurs every other day (bi-daily). Administration can occur on one or more days.
[0102] Administration of the compositions and dosage forms can be combined with other regimens used for treatment of the condition. For example, the method of the present invention can be combined with diet regimens (e.g., low carbohydrate diets, high protein diets, high fiber diets, etc.), exercise regimens, weight loss regimens, smoking cessation regimens, or combinations thereof. The method of the present invention can also be used in combination with other pharmaceutical products in the treatment of the condition. The compositions or dosage forms of the present invention can be administered before or after other regimens or pharmaceutical products.
Kits Comprising the Compositions
[0103] The invention is directed to kits or packages containing one or more units of a composition of the invention. Kits or packages can include units of a food product, pharmaceutical composition, cosmetic, or industrial composition comprising the microorganism, biomass, or microbial oil of the invention, or combinations thereof. Kits or packages can also include an additive comprising the microorganism, biomass, or microbial oil of the invention, or combinations thereof for preparation of a food, cosmetic, pharmaceutical composition, or industrial composition.
[0104] In some embodiments, the kit or package contains one or more units of a pharmaceutical composition to be administered according to the methods of the present invention. The kit or package can contain one dosage unit, or more than one dosage unit (i.e., multiple dosage units). If multiple dosage units are present in the kit or package, the multiple dosage units can be optionally arranged for sequential administration.
[0105] The kits of the present invention can optionally contain instructions associated with the units or dosage forms of the kits. Such instructions can be in a form prescribed by a governmental agency regulating the manufacture, use or sale of pharmaceutical products, which notice reflects approval by the agency of the manufacture, use or sale for human administration to treat a condition or disorder. The instructions can be in any form which conveys information on the use of the units or dosage forms in the kit according to the methods of the invention. For example, the instructions can be in the form of printed matter, or in the form of a pre-recorded media device.
|01061 In the course of examination of a patient, a medical professional can determine that administration of one of the methods of the present invention is appropriate for the patient, or the physician can determine that the patient's condition can be improved by the administration of one of the methods of the present invention. Prior to prescribing any regimen, the physician can counsel the patient, for example, on the various risks and benefits associated with the regimen. The patient can be provided full disclosure of all known and suspected risks associated with the regimen. Such counseling can be provided verbally, as well as in written form. In some embodiments, the physician can provide the patient with literature materials on the regimen, such as product information, educational materials, and the like.
[0107] The present invention is directed to methods of educating consumers about the methods of treatment, the method comprising distributing the dosage forms with consumer information at a point of sale. In some embodiments, the distribution will occur at a point of sale having a pharmacist or healthcare provider.
[0108] The term "consumer information" can include, but is not limited to, an English language text, non-English language text, visual image, chart, telephone recording, website, and access to a live customer service representative. In some embodiments, consumer information will provide directions for use of the dosage forms according to the methods of the present invention, appropriate age use, indication, contraindications, appropriate dosing, warnings, telephone number or website address. In some embodiments, the method further comprises providing professional information to relevant persons in a position to answer consumer questions regarding use of the disclosed regimens according to the methods of the present invention. The term "professional information" includes, but is not limited to, information concerning the regimen when administered according to the methods of the present invention that is designed to enable a medical professional to answer costumer questions. A "medical professional," includes, for example, a physician, physician assistant, nurse, nurse practitioner, pharmacist and customer service representative.
Having generally described this invention, a further understanding can be obtained by reference to the examples provided herein. These examples are for purposes of illustration only and are not intended to be limiting.
EXAMPLE 1
Isolation of Microorganisms ] Samples were collected from intertidal habitats during low tide, including bays and estuaries along the West Coast of North America (California, Oregon, and Washington) and Hawaii. Water, sediment, living plant material, and decaying plant/animal debris were placed into sterile 50 ml tubes. Portions of each sample along with the water were spread onto solid agar plates of isolation media. Isolation media consisted of: 500 ml of artificial seawater, 500 ml of distilled water, 1 g of glucose, 1 g of glycerol, 13 g of agar, 1 g of glutamate, 0.5 g of yeast extract, 0.5 g casein hydrolysate, 1 ml of a vitamin solution (100 mg/L thiamine, 0.5 mg/L biotin, 0.5 mg B\ 2), 1 ml of a trace mineral solution (PII metals, containing per liter: 6.0 g FeCWHiO, 6.84 g H3BO3, 0.86 g MnCl24H20, 0.06 g ZnCl2, 0.026 CoCl26H20, 0.052 g NiS04H20, 0.002 g CuS045H20 and 0.005 g Na2Mo042H20), and 500 mg each of penicillin G and streptomycin sulfate. The agar plates were incubated in the dark at 20-25°C. After 2-4 days the agar plates were examined under magnification, and colonies of cells were picked with a sterile toothpick and restreaked onto a fresh plate of media. Cells were repeatedly streaked onto fresh media until contaminated organisms were removed. Two of the isolated microorganisms were deposited under ATCC Accession Nos. PTA- 10212 and PTA- 10208.
1 axonomic Characteristics of the Isolated Microorganism Deposited Under ATCC
Accession No. PTA-10212 ] Cultures of the isolated microorganism deposited under ATCC Accession No.
PTA-10212 ("PTA-10212") appeared as white, wet, smeared colonies without visible isolated sori. 101 131 PTA-10212 was grown on solid and liquid FFM, solid KMV, KMV slush (1%),
KMV broth, and MH broth to further examine growth characteristics. PTA-10212 was observed to grow rapidly on KMV and MH. See, e.g., Porter D., 1989. Phylum Labyrinthiilomycota. In Margulis, L., Corliss, J.O., Melkonian, M., Chapman, D.J. (Eds.) Handbook of Protoctista, Jones and Bartlett, Boston, pp. 388-398 (KMV); Honda et al, Mycol. Res. 702:439-448 (1998) (MH); and U.S. Patent No. 5, 130,242 (FFM), each of which is incorporated herein by reference in its entirety.
[0114] The following observations were made after growth of PTA- 10212 over several days on solid FFM media, after 72 hours growth in KMV medias, and MH broth. Sporangia were not clumped in/on any media and were very small (5- 10 μηι). PTA- 10212 did not demonstrate the copious tetrads characteristic of Schizochytrium cleavage patterns. Amoeboid cells appeared about 24 hours after transfer to fresh solid media. These amoeboid cells were gone after a few days and were not evident in liquid or slush media. Unlike Aurantiochytrium, described by Yokoyama, R. et al., Mycoscience 48(6): 329-341 (2007), as having the appearance of "small sandgrains on the bottom of the flask" when grown in liquid media, PTA-10212 did not settle at the bottom of the flask but was suspended in both KMV and MH liquid media. The sporangia were not as dense as typical of Schizochytrium or Oligochytrium, which also have robust ectoplasmic networks that were absent from PTA- 10212. While most species undergo vegetative cleavage of small sporangia or assimilative cells by the division of a larger sporangium over several hours, PTA-10212 formed dumbbell-shaped elongated assimilative cells, which then formed a thin isthmus that pulled apart as the ends of the dumbbell separated. The resulting cells appeared to be small assimilative cells. Direct transformation of an amoeboid cell into the dumbbell shaped assimilative cell was not observed. Typical biflagellate zoospores were observed swimming but were relatively rare. PTA-10212 was non-prolific, dividing by vegetative cleavage. Direct release of zoospores was not observed, although zoospores were observed swimming. Vegetative cells were very small (2 μηι to 5 μιη).
[0115] PT A- 10212 was further examined using the flow-through technique, in which microscopic slides were prepared by suspending a small portion of an agar-grown colony in a drop of half-strength sea water. With this technique, primary sporangia were observed to be globose and approximately 10 μιη in diameter. Walls were very thin and remnants were not observed when binary division of the protoplast was initiated. Repeated binary division produced 8-16 smaller (4-5 μηι in diameter) secondary sporangia. The secondary sporangia remained quiescent for several hours before again releasing an amorphous protoplast. The amorphous protoplast divided by pinching and pulling, initially producing typical dumbbell-shaped intermediate stages and finally resulting in 4-8 small globose bodies 2.5-2.8 μηι in diameter. The latter rested for several minutes up to 1-2 hours, then changed shape (elongated) and turned into biflagellate zoospores, 2.3-2.5 x 3.7-3.9 μηι. Zoospores were abundant and could be precisely measured when they came to rest. Zoospores then rounded off and started a new cycle of development. The zoospores were larger than Sicyoidochytrium minutum and smaller than Ulkenia visurgensis.
] PTA-10212 was further characterized based on the similarity of its 18s rRNA gene to that of known species. Genomic DNA was prepared from PTA-10212 by standard procedures. See, for example, Sambrook J. and Russell D. 2001. Molecular cloning: A laboratory manual, 3rd edition. Cold Spring Harbor Laboratory Press, Cold Spring Harbor, New York. Briefly: (1) 500 xL of cells were centrifuged from mid-log culture. The cells were re-centrifuged, and all traces of liquid were removed from the cell pellet with a small-bore tip; (2) pellets were resuspended with 200 μΐ^ lysis buffer (20 mM Tris pH 8.0, 125 μg/mL Proteinase K, 50 niM NaCl, 10 niM EDTA pH 8.0, 0.5% SDS); (3) cells were lysed at 50°C for 1 hour; (4) the lysis mixture was pipetted into phase-lock gel (PLG-Eppendorf) 2 mL tubes; (5) equal volume of P:C:I was added and allowed to mix for 1.5 hours; (6) the tubes were centrifuged at 12,000 x g for 5 minutes; (7) the aqueous phase was removed from above the gel within the PLG tube and an equal volume of chloroform was added to the aqueous phase, and mixed for 30 minutes; (8) the tubes were centrifuged at 14,000 x g for approximately 5 minutes; (9) the top layer (aqueous phase) was pipetted away from the chloroform, and placed in a new tube; (10) 0.1 volume of 3 M NaOAC was added and mixed (inverted several times); (1 1) 2 volumes of 100% EtOH were added and mixed (inverted several times) with genomic DNA precipitant forming at this stage; (12) the tubes were centrifuged at 4°C in a microcentrifuge at 14,000 x g for approximately 15 minutes; (13) the liquid was gently poured off with genomic DNA remaining at the bottom of the tube; (14) the pellet was washed with 0.5 mL 70%> EtOH; (15) the tubes were centrifuged at 4°C in a microcentrifuge at 14,000 x g for approximately 5 minutes; (16) the EtOH was gently poured off and the genomic DNA pellet was dried; and (17) a suitable volume of H20 and RNase was added directly to the genomic DNA pellet. The PCR amplification of the 18s rRNA gene was carried out with primers previously described (Honda et. al, J. Euk. Micro. 46(6): 637-647 (1999). The PCR conditions with chromosomal DNA template were as follows: 0.2 μΜ dNTPs, 0.1 μΜ each primer, 8% DMSO, 200 ng chromosomal DNA, 2.5 U Herculase® II Fusion DNA Polymerase (Stratagene), and Herculase® buffer (Stratagene) in a 50 μΐ, total volume. The PCR Protocol included the following steps: (1) 95°C for 2 minutes; (2) 95°C for 35 seconds; (3) 55°C for 35 seconds; (4) 72°C for 1 minute and 30 seconds; (5) repeat steps 2-4 for 30 cycles; (6) 72°C for 5 minutes; and (7) hold at 4°C.
] PCR amplification yielded a distinct DNA product with the expected size using chromosomal template described above. The PCR product was cloned into the vector pJET1.2/blunt (Fermentas) according to the manufacturer's instructions, and the insert sequence was determined using supplied standard primers.
] Phylo genetic analysis places PTA-10212 within the lineage that includes
Thranstochytrium pachydermum and Thraustochytrium aggregatum with moderate support. The sporangia of T. pachydermum have very thick cell walls. T. aggregatum forms clearly visible clumps of sori that are opaque. PTA-10212 shows neither of these characteristics. The presence of many amoeboid cells has been described in other taxa, such as Ulkenia, T. gaertnerium, A. limiacinum, and S. mangrovei; however, the descriptions associated with those taxa differ from the observed characteristics of the isolate. Moreover, PTA-10212 did not show phylogenetic affinity towards any of these taxa.
] Table 3 shows a comparison of the 18s rRNA sequence from the microorganism deposited under ATCC Accession No. PTA-10212 to DNA sequences in the National Center for Biotechnology Information (NCBI) electronic database. The percent identity was determined using two different calculations. "Calculation #1" takes into consideration any "gaps" that occur in the sequences, either from non-homologous regions or partial sequence (AlignX-VectorNTI default settings). "Calculation #2" does not include calculated penalties for gaps (AlignX-VectorNTI "IDENTITY" matrix setting). Table 3: Comparison of 1 8s rRNA Sequences
Figure imgf000044_0001
(p): indicates partial sequence
[0120] As shown in Table 3, it was found that, in terms of % identity, the 18s rRNA gene sequence (SEQ ID NO: l) from the microorganism deposited under ATCC Accession No. PTA-10212 is related, though not identical, to 18s rRNA gene sequences available in the NCBI database. It is generally recognized that organisms can have closely related 18s rRNA gene sequences while belonging to a different genus or species.
[0121] Based on the above characterization, the isolated microorganism deposited under
ATCC Accession No. PTA-10212 is believed to represent a new Thraustochytrium species and is therefore also designated as Thraustochytrium sp, ATCC PTA-10212.
Taxonomic Characteristics of the Isolated Microorganism Deposited Under ATCC Accession No. PTA-10208
[0122] The microorganism deposited under ATCC Accession No. PTA-10208 ("PTA-
10208") was identified as a sub-isolate (an individual cell isolated from a culture and maintained as a new separate and distinct culture) of the microorganism deposited under ATCC Accession No. PTA-9695 ("PTA-9695"), described in U.S. Appl. No. 12/407,687 and PCT/US2009/001720, each of which is incorporated herein by reference in its entirety.
[0123] PTA-10208 shares taxonomic characteristics with PTA-9695. PTA-9695 was found to have biflagellate zoospores at discharge that swim actively away from the mature sporangium, wall remnants of which were clearly visible (in phase contrast) after spore release. PTA-9695 sporangia measured 12.5 μηι to 25 μηι in diameter, and zoospores were 2.5 μηι to 2.8 μηι x 4.5 μηι to 4.8 μηι in size. There were 8 to 24 spores per individual PTA-9695 sporangium. Settled PTA-9695 zoospores enlarged and rapidly underwent binary divisions leading to tetrads, octads, and finally to clusters of sporangia. Tetrad formation commenced at a very early stage prior to maturity of the sporangia. These characteristics are in agreement with the genus Schizochytriiim. In terms of % identity, the PTA-9695 18s rRNA gene sequence (SEQ ID NO:2), which is shared by PTA- 10208, was found to be closely related, though not identical, to the 18s rRNA gene sequence of T. aggregation provided in Honda, D. et al., J. Euk. Micro. 46(6): 637-647 (1999). The 18s rRNA sequence published for Thraustochytrium aggregation is a partial sequence, with an approximately 71 DNA nucleotide gap in the middle of the sequence. PTA-9695 is believed to represent a new Schizochytrium species. As such, the sub- isolate PTA- 10208 is also designated as Schizochytrium sp. ATCC PTA- 10208.
EXAMPLE 2
Growth Characteristics of the Isolated Microorganism Deposited Under ATCC Accession No. PTA-10212
[0124] The isolated microorganism deposited under ATCC Accession No. PTA-10212 was examined for growth characteristics in individual fermentation runs, as described below. Typical media and cultivation conditions are shown in Table 1.
[0125] In carbon (glycerol) and nitrogen-fed cultures with 1000 ppm CI" at 22.5°C with
20% dissolved oxygen at pH 7.3, PTA-10212 produced a dry cell weight of 26.2 g/L after 138 hours of culture in a 10 L fermentor volume. The lipid yield was 7.9 g/L; the omega- 3 yield was 5.3 g/L; the EPA yield was 3.3 g/L; and the DHA yield was 1.8 g/L. The fatty acid content was 30.3% by weight; the EPA content was 41.4% of fatty acid methyl esters (FAME); and the DHA content was 26.2% of FAME. The lipid productivity was 1.38 g/L/day, and the omega-3 productivity was 0.92 g/L/day under these conditions, with 0.57 g/L/day EPA productivity and 0.31 g/L/day DHA productivity.
[0126] In carbon (glycerol) and nitrogen-fed cultures with 1000 ppm CI at 22.5°C with
20% dissolved oxygen at pH 7.3, PTA-10212 produced a dry cell weight of 38.4 g/L after 189 hours of culture in a 10 L fermentor volume. The lipid yield was 18 g/L; the omega- 3 yield was 12 g/L; the EPA yield was 5 g/L; and the DHA yield was 6.8 g/L. The fatty acid content was 45% by weight; the EPA content was 27.8% of FAME; and the DHA content was 37.9% of FAME. The lipid productivity was 2.3 g/L/day, and the omega-3 productivity was 1.5 g/L/day under these conditions, with 0.63 g/L/day EPA productivity and 0.86 g/L/day DHA productivity.
[0127] In carbon (glycerol) and nitrogen-fed cultures with 1000 ppm CI" at 22.5°C with
20% dissolved oxygen at pH 6.8-7.7, PTA-10212 produced a dry cell weight of 13 g/L after 189 hours of culture in a 10 L fermentor volume. The lipid yield was 5.6 g/L; the omega-3 yield was 3.5 g/L; the EPA yield was 1.55 g/L; and the DHA yield was 1.9 g/L. The fatty acid content was 38% by weight; the EPA content was 29.5% of FAME; and the DHA content was 36% of FAME. The lipid productivity was 0.67 g/L/day, and the omega-3 productivity was 0.4 g/L/day under these conditions, with 0.20 g/L/day EPA productivity and 0.24 g/L/day DHA productivity.
[0128] In carbon (glycerol) and nitrogen-fed cultures with 1000 ppm CI" at 22.5-28.5°C with 20% dissolved oxygen at pH 6.6-7.2, PTA-10212 produced a dry cell weight of 36.7 g/L - 48.7 g/L after 191 hours of culture in a 10 L fermentor volume. The lipid yield was 15.2 g/L - 25.3 g/L; the omega-3 yield was 9.3 g/L - 13.8 g/L; the EPA yield was 2.5 g/L - 3.3 g/L; and the DHA yield was 5.8 g/L - 1 1 g/L. The fatty acid content was 42.4% - 53% by weight; the EPA content was 9.8% - 22% of FAME; and the DHA content was 38.1 % - 43.6% of FAME. The lipid productivity was 1.9 g/L/day - 3.2 g/L/day, and the omega-3 productivity was 1.2 g/L/day - 1.7 g/L/day under these conditions, with 0.31 g/L/day - 0.41 g/L/day EPA productivity and 0.72 g/L/day - 1.4 g/L/day DHA productivity.
Growth Characteristics of the Isolated Microorganism Deposited Under ATCC Accession No. PTA-10208
[0129] The isolated microorganism deposited under ATCC Accession No. PTA- 10208 was examined for growth characteristics in individual fermentation runs, as described below. Typical media and cultivation conditions are shown in Table 2.
[0130] In carbon (glucose) and nitrogen-fed cultures with 1000 ppm CI" at 22.5°C at pH
7.0 with 20% dissolved oxygen during the nitrogen feed and 10% dissolved oxygen thereafter, PTA- 10208 produced a dry cell weight of 95 g/L after 200 hours of culture in a 10 L fermentor volume. The lipid yield was 53.7 g/L; the omega-3 yield was 37 g/L; the EPA yield was 14.3 g/L; and the DHA yield was 21 g/L. The fatty acid content was 57% by weight; the EPA content was 27.7% of FAME; and the DHA content was 39.1 % of FAME. The lipid productivity was 6.4 g/L/day, and the omega-3 productivity was 4.4 g/L/day under these conditions, with 1.7 g/L/day EPA productivity and 2.5 g/L/day DHA productivity.
[0131 ] In carbon (glucose) and nitrogen-fed cultures with 1000 ppm CI" at 22.5°C at pH
7.5 with 20% dissolved oxygen during the nitrogen feed and 10% dissolved oxygen thereafter, PTA-10208 produced a dry cell weight of 56 g/L after 139 hours of culture in a 10 L fermentor volume. The lipid yield was 53 g/L; the omega-3 yield was 34 g/L; the EPA yield was 1 1.5 g/L; and the DHA yield was 22 g/L. The fatty acid content was 58% by weight; the EPA content was 21.7% of FAME; and the DHA content was 41.7% of FAME. The lipid productivity was 9.2 g/L/day, and the omega-3 productivity was 5.9 g/L/day under these conditions, with 2 g/L/day EPA productivity and 3.8 g/L/day DHA productivity.
[0132] In carbon (glucose) and nitrogen-fed cultures with 1000 ppm CI" at 22.5°C at pH
7.0 with 20% dissolved oxygen during the nitrogen feed and 10% dissolved oxygen thereafter, PTA-10208 produced a dry cell weight of 93.8 g/L after 167 hours of culture in a 2000 L fermentor volume. The lipid yield was 47.2 g/L; the omega-3 yield was 33.1 g/L; the EPA yield was 10.5 g/L; and the DHA yield was 20.4 g/L. The fatty acid content was 50.6%) by weight; the EPA content was 23% of FAME; and the DHA content was 42.6% of FAME. The lipid productivity was 6.8 g/L/day, and the omega-3 productivity was 4.7 g/L/day under these conditions, with 1.5 g/L/day EPA productivity and 2.9 g/L/day DHA productivity.
[0133] In carbon (glucose) and nitrogen-fed cultures with 1000 ppm Cf at 22.5°C at pH
7.0 with 20% dissolved oxygen during the nitrogen feed and 10% dissolved oxygen thereafter, PTA-10208 produced a dry cell weight of 105 g/L after 168 hours of culture in a 2000 L fermentor volume. The lipid yield was 46.4g/L; the omega-3 yield was 33 g/L; the EPA yield was 10.7 g/L; and the DHA yield was 20.3 g/L. The fatty acid content was 43.9% by weight; the EPA content was 24% of FAME; and the DHA content was 43.7% of FAME. The lipid productivity was 6.6 g/L/day, and the omega-3 productivity was 4.7 g/L/day under these conditions, with 1.5 g/L/day EPA productivity and 2.9 g/L/day DHA productivity. [0134] In carbon (glucose) and nitrogen-fed cultures with 1000 ppm CI" at 22.5°C at pH
7.0 with 20% dissolved oxygen during the nitrogen feed and 10% dissolved oxygen thereafter, PTA-10208 produced a dry cell weight of 64.8 g/L after 168 hours of culture in a 2000 L fermentor volume. The lipid yield was 38.7 g/L; the omega-3 yield was 29.9 g/L; the EPA yield was 8.5 g/L; and the DHA yield was 16.7 g/L. The fatty acid content was 59.6% by weight; the EPA content was 23% of FAME; and the DHA content was 42.3%> of FAME. The lipid productivity was 5.53 g/L/day, and the omega-3 productivity was 3.8 g/L/day under these conditions, with 1.2 g/L/day EPA productivity and 2.3 g/L/day DHA productivity.
EXAMPLE 3
Fatty Acid Profiles of Microorganism Strains ATCC PTA-10208 and PTA-10212
[0135] Four samples of biomass (PTA-10208 Sample #1 ; PTA-10208 Sample #2; PTA-
10212 Sample #1 ; and PTA-10212 Sample #2) were analyzed for total crude oil content by solvent extraction, lipid classes were determined by high performance liquid chromatography/evaporative light scattering detection (HPLC/ELSD), triacylglycerol (TAG) were analyzed by HPLC/mass spectrometry (HPLC/MS), and fatty acid (FA) profiles were determined by gas chromatography with flame ionization detection (GC- FID). The cmde lipid content of each freeze dried biomass was determined using solvent grinding with hexane and compared to the sum of FAME (mg/g) generated by direct transesterification, and the resultant fatty acid methyl esters (FAME) were quantified by GC/FID analysis. Fatty acids in the extracted crude lipid were also quantified by transesterification and quantified using GC/FID analysis of the resultant FAME. The weight percent of all neutral lipids (NL) and free fatty acids (FFA) were determined in the extracted crude lipid using normal phase HPLC with ELSD and atmospheric pressure chemical ionization-MS (APCI-MS) identification. The method separates and quantifies sterol esters (SE), TAG, free fatty acids (FFA), 1,3-diacylglycerols (1, 3-D AG), sterols, 1,2-diacylglycerols (1 ,2-DAG), and monoacylglycerols (MAG). Results are shown in Tables 4 and 5, below. [0136] TAG and phospholipids (PL) were isolated from the crude oils extracted from the four samples of biomass (PTA-10208 Sample #1 ; PTA-10208 Sample #2; PTA-10212 Sample #1 ; and PTA-10212 Sample #2). TAG was isolated using low pressure flash chromatography and PL was isolated using solid phase extraction (SPE). The identity of each isolated fraction was confirmed by thin layer chromatography (TLC). The fatty acid profiles of the isolated TAG and PL fractions were determined following direct transesterification using GC-FID as FAME. Results are shown in Tables 6 and 7, below.
[0137] The total crude oil content and fatty acid profiles of isolated lipid classes were also determined for two additional samples of biomass from microorganism strain ATCC PTA-10212 (PTA-10212 Sample #3 and PTA-10212 Sample #4). Crude oil was obtained from each sample by hexane extraction, and individual lipid classes were isolated using low pressure flash chromatography. The fatty acid profiles of the biomass, crude oil, and isolated fractions were determined using GC-FID as FAME. Results are shown in Tables 8-1 1, below.
[0138] Individual lipid classes were isolated from a sample of crude oil from microorganism strain ATCC PTA-10212 (PTA-10212 Sample #5) previously extracted using the FRIOLEX® process, and the fatty acid profiles of each class were determined using GC-FID as FAME. Results are shown in Tables 12 and 13, below.
[0139] Individual lipid classes were isolated from a sample of crude oil from microorganism strain ATCC PTA-10208 (PTA-10208 Sample #3) using normal HPLC with ELSD and APCI-MS identification.
Experimental Procedures
[0140] Crude Oil Extraction - Crude oil was extracted from samples of freeze-dried biomass using solvent grinding. For example, approximately 3 grams of biomass was weighed into a Swedish tube. Three ball bearings and 30 mL of hexane were added to the Swedish tube, which was sealed with a neoprene stopper and placed in a shaker for 2 hours. The resultant slurry was filtered using a Buchner funnel and Whatman filter paper. The filtered liquid was collected, the solvent removed under vacuum, and the amount of remaining crude lipid determined gravimetrically.
[0141] Fatty Acid Analysis - The samples of biomass, extracted crude lipid, and isolated lipid classes were analyzed for fatty acid composition as FAME. Briefly, freeze-dried biomass and isolated lipid classes were weighed directly into a screw cap test tubes, while samples of the crude oil were dissolved in hexane to give a concentration of approximately 2 mg/mL. Toluene, containing internal standard, and 1.5 N HC1 in methanol was added to each tube. The tubes were vortexed, then capped and heated to 100° C for 2 hours. The tubes were allowed to cool, and saturated NaCl in water was added. The tubes were vortexed again and centrifuged to allow the layers to separate. A portion of the organic layer was then placed in a GC vial and analyzed by GC-FID. FAME was quantified using a 3 -point calibration curve generated using Nu-Check-Prep GLC Reference Standard (NuCheck, Elysian, MN). Fatty acids present in the extract were expressed as mg/g and as a weight percent. Fat content in the samples was estimated assuming equal response to the internal standard when analyzed by GC-FID.
HPLC/ELSD/MS Method -
Instrument Agilent 1100 HPLC, Alltech 3300 ELSD, Agilent 1100
MSD
Column Phenomenex Luna Silica, 250 x 4.6 mm,
5 μιη particle size w/ Guard Column
Mobile Phase A - 99.5% Hexanes (Omnisolv)
0.4% Isopropyl alcohol (Omnisolv)
0.1% Acetic Acid
B - 99.9% Ethanol (Omnisolv, 95:5 Ethanol:IPA)
0.1% Acetic Acid
Gradient
Figure imgf000050_0001
Column Temp. 30°C
Flow Rate 1.5 mL/min
Injection Volume 5
ELSD Detection Temperature 35°C, Gas flow 1.2 L/min
MSD Mass Range 200 - 1200, Fragmentor 225 V
Drying Gas Temperature 350°C
Vaporizer Temperature 325°C
Capillary Voltage 3500 V
Corona Current 10 μ A [0143] Solid Phase Extraction -PL fractions were separated from the crude lipid by solid phase extraction (SPE) using 2 g aminopropyl cartridges (Biotage, Uppsala, Sweden) placed in a Vac Elut apparatus (Varian Inc, Palo Alto, USA). The cartridge was conditioned with 15 mL of hexane, and -60 mg of each sample was dissolved in 1 mL CHCI3 and applied to the cartridge. The column was washed with 15 mL of 2: 1 CHCl3:isopropyl alcohol to elute all the neutral lipids, which was discarded. The fatty acids were then eluted with 15 mL of 2% acetic acid (HO Ac) in ether, which was discarded. The PL portion was eluted with 15 mL of 6: 1 Methanol : Chloroform, which was collected, dried under nitrogen, and weighed.
[0144] Flash Chromatography - Flash chromatography was used to separate the lipid classes present in the crude oil. Approximately 200 mg of crude oil dissolved in hexane was injected onto the head of the column. The chromatography system utilized Silica Gel 60 (EMD Chemical, Gibbstown, NJ) with mobile phase composed of Petroleum Ether and Ethyl Acetate at 5 mL/min (Tables 6-7) or 3 mL/min (Tables 8-13). A step gradient was used to selectively elute each lipid class from the column. The mobile phase gradient started from 100% petroleum ether and finished with 50% ethyl acetate. Fractions were collected in 10 mL test tubes using a Gilson FC 204 large-bed fraction collector (Gilson, Inc., Middleton, WI). Each tube was analyzed by thin layer chromatography (TLC) and the tubes containing individual lipid classes (as judged by single spots on TLC plate with expected retention factor (Rf)) were pooled, concentrated to dryness, and weighed. The total fraction content was then determined gravimetrically.
[0145] TLC Analysis - Thin layer chromatography was conducted on silica gel plates.
The plates were eluted using a solvent system consisting of petroleum ether : ethyl ether : acetic acid (80:20:1) and were visualized using iodine vapor. The Rf values of each spot were then compared with reported literature values for each lipid class.
[0146] Analysis of TAG and PL fractions - The isolated TAG and PL fractions were analyzed for fatty acid composition as fatty acid methyl esters (FAME). The TAG fractions were dissolved in hexane to give a concentration of approximately 1 -2 mg/mL. 1 mL aliquots of the solutions were concentrated to dryness under nitrogen. Toluene, containing internal standard, and 1.5 N HC1 in methanol was added to each tube. The tubes were vortex ed, then capped and heated to 100° C for 2 hours. Internal standard and HC1 methanol were added directly to the tubes containing the PL fraction and heated. The tubes were allowed to cool, and saturated NaCl in water was added. The tubes were vortexed again and centrifuged to allow the layers to separate. A portion of the organic layer was then placed in a GC vial and analyzed by GC-FID. FAMEs were quantified using a 3 -point calibration curve generated using Nu-Check-Prep GLC 502B Reference Standard (NuCheck, Elysian, MN). Fatty acids present in the extract were expressed as mg/g and as a % of FAME.
Results
PT A- 10208 Sample #1
[0147] The fatty acid profile of the biomass and extracted crude lipid for PTA-10208
Sample #1 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 28.6 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 55.0 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 53.2% (as SUM of FAME) using GC with FID detection, while 52.0% (wt/wt) lipid was extracted from the dry biomass, giving a 97.8% recovery of total lipid. The crude lipid was determined to be 91.9% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were C16:0 (182.5 mg/g), C20:5 n-3 (186.8 mg/g), and C22:6 n-3 (423.1 mg/g).
[0148] The lipid class profile of the extracted crude lipid was determined by weighing
55.0 mg of crude lipid into a 50 mL volumetric flask and transferring an aliquot into an HPLC vial for HPLC/ELSD/MS analysis. According to the HPLC/ELSD/MS analysis, the crude lipid contained 0.2% sterol esters (SE), 95.1 % TAG, 0.4% sterols, and 0.5% 1,2-diacylglycerol (DAG). 5% of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
[0149] Isolated TAG from this sample as determined by flash chromatography made up approximately 92.4% of the crude oil. PL was not detected by weight or TLC after SPE isolation. The major fatty acids (>50 mg/g) contained in the TAG were C I 6:0 (189 mg/g), C20:5 n-3 (197 mg/g), and C22:6 n-3 (441 mg/g). PTA-10208 Sample #2
[0150] The fatty acid profile of the biomass and extracted crude lipid for PTA-10208
Sample #2 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 32.0 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 60.1 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 52.4% (as SUM of FAME) using GC with FID detection, while 48.0% (wt/wt) lipid was extracted from the dry biomass, giving a 91.7% recovery of total lipid. The crude lipid was determined to be 95.3% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were C16:0 (217.5 mg/g), C20:5 n-3 (169.3 mg/g), and C22:6 n-3 (444.1 mg/g).
[0151] The lipid class profile of the extracted crude lipid was determined by weighing
60.1 mg of crude lipid into a 50 mL volumetric flask and transferring an aliquot into an HPLC vial for HPLC/ELSD/MS analysis. According to the HPLC/ELSD/MS analysis, the crude lipid contained 0.2% SE, 95.7% TAG, 0.3% sterols, and 0.7% 1,2-DAG. 5.1 % of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
[0152] Isolated TAG from this sample made up approximately 93.9% of the crude oil.
PL was not detected by weight or TLC after SPE isolation. The major fatty acids (>50mg/g) contained in the TAG were C I 6:0 (218 mg/g), C20:5 n-3 (167 mg/g) and C22:6 n-3 (430 mg/g).
PTA-10208 Sample #3
[0153] A sample of crude oil from the microorganism deposited under ATCC Accession
No. PTA-10208 (Sample PTA-10208 #3) was analyzed using HPLC/ELSD/MS. A total of 98.38%o of lipids were recovered, with the sterol ester (SE) fraction accounting for 0.32%, the TAG fraction accounting for 96.13%, the 1 ,3-diacylglycerol (DAG) fraction accounting for 0.22%, the 1 ,2-DAG fraction accounting for 0.78%, and the sterol fraction accounting for 0.93%. PTA-10212 Sample #1
[015 1 The fatty acid profile of the biomass and extracted crude lipid for PTA-10212
Sample #1 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 27.0 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 52.5 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 38.3% (as SUM of FAME) using GC with FID detection, while 36.3% (wt/wt) lipid was extracted from the dry biomass, giving a 94.6% recovery of total lipid. The crude lipid was determined to be 83.2% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were CI 6:0 (328.5 mg/g), C20:5 n-3 (90.08 mg/g), and C22:6 n-3 (289.3 mg/g).
[0155] The lipid class profile of the extracted crude lipid was determined by weighing
52.5 mg of crude lipid into a 50 mL volumetric flask and transferring an aliquot into an HPLC vial for HPLC/ELSD/MS analysis. According to the HPLC/ELSD/MS analysis, the crude lipid contained 0.2% SE, 64.2% TAG, 1.9% FFA, 2.8% 1 ,3-DAG, 1.4% sterols, 18.8% 1 ,2-DAG, and 0.5% MAG. 3.4% of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
[0156] Isolated TAG from this sample made up approximately 49.8% of the crude oil.
Isolated PL made up approximately 8.1 % of the crude oil. The major fatty acids (>50mg/g) contained in the TAG fraction are C16:0 (400 mg/g), C20:5 n-3 (91 mg/g), and C22:6 n-3 (273 mg/g). The major fatty acids (>50mg/g) contained in the PL fraction are C16:0 (98 mg/g), C20:5 n-3 (33 mg/g), and C22:6 n-3 (227 mg/g).
PTA-10212 Sample #2
[0157| The fatty acid profile of the biomass and extracted crude lipid PTA- 10212 Sample
#2 was determined using GC/FID. Fatty acids in the biomass were transesterified in situ by weighing 29.5 mg of biomass directly into a FAME tube, while a sample of the extracted crude lipid was prepared by weighing 56.5 mg of crude lipid into a 50 mL volumetric flask and transferring 1 ml to a separate FAME tube. The estimated crude lipid content of the biomass was determined to be 40.0% (as SUM of FAME) using GC with FID detection, while 41.3% (wt/wt) lipid was extracted from the dry biomass, giving a 106.1 % recovery of total lipid. The crude lipid was determined to be 82.8% fatty acids (as SUM of FAME) using GC/FID. The major fatty acids contained in the crude lipid were C16:0 (327.3 mg/g), C20:5 n-3 (92.5 mg/g), and C22:6 n-3 (277.6 mg/g).
[0158] The lipid class profile of the extracted crude lipid was determined by weighing
56.5 mg of crude lipid into a 50 mL volumetric flask and transferring an aliquot into an HPLC vial for HPLC/ELSD/MS analysis. According to the HPLC/ELSD/MS analysis, the crude lipid contained 0.2% SE, 58.2% TAG, 2.3% FFA, 3.4% 1,3-DAG, 1.7% sterols, 23.4% 1 ,2-DAG, and 0.6% MAG. 3.3% of the TAG fraction included a peak that eluted directly after the TAG peak, but did not give a recognizable mass spectrum.
[0159] Isolated TAG from this sample made up approximately 51.9% of the crude oil.
Isolated PL made up approximately 8.8% of the crude oil. The major fatty acids (>50mg/g) contained in the TAG fraction are CI 6:0 (402 mg/g), C20:5 n-3 (92 mg/g), and C22:6 n-3 (245 mg/g). The major fatty acids (>50mg/g) contained in the PL fraction are C16:0 (121 mg/g), C20:5 n-3 (48 mg/g), and C22:6 n-3 (246 mg/g).
Fatty Acid Profiles of PTA- 10208 and PTA- 10212 Biomasses and
Extracted Crude Lipids (mg/g)
PTA- PTA- PTA- PTA- PTA- PTA- PTA- PTA- 10208 10208 10208 10208 10212 10212 10212 10212 Sample Sample #1 Sample Sample #2 Sample Sample #1 Sample Sample #2 #1 #2 #1 #2
Crude Crude Crude
Biomass Lipid Biomass Lipid Biomass Lipid Biomass Crude Lipid
Fatty FAME FAME FAME FAME FAME FAME FAME FAME Acid (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g) (mg/g)
C I 2:0 1 .47 2.43 1.80 3.14 0.99 1.90 0.87 1.91
C 14:0 1 1 .62 20.12 16.72 31.03 5.51 12.91 5.97 13.69
C14: l 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
C15:0 2.43 3.75 3.60 6.22 9.13 20.42 9.39 20.81
C16:0 105.04 182.47 1 17.72 217.49 145.87 328.45 147.87 327.27
C16: l 0.00 0.00 0.06 0.01 6.26 14.53 7.46 16.89
C 18:0 5.37 8.96 4.77 8.37 6.77 15.39 6.77 15.15
C18: l
0.00 3.26 0.00 3.09 0.03 4.04 0.08 5.87 n-9
C18: l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-7
C18:2
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C20:0 1.48 1.79 1.40 1.85 1.60 3.09 1.67 3.20
CI 8:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-3
C20: l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
CI 8:4
0.91 1 .61 1. 10 2.00 2.28 2.56 2.21 2.64 n-3 PTA- PTA- PTA- PTA- PTA- PTA- PTA- PTA- 10208 10208 10208 10208 10212 10212 10212 10212 Sample Sample #1 Sample Sample #2 Sample Sample #1 Sample Sample #2 #1 #2 #1 #2
Crude Crude Crude
Biomass Lipid Biomass Lipid Biomass Lipid Biomass Crude Lipid
C20:2
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C20:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C22:0 0.10 0.00 0.08 0.00 0.30 0.12 0.35 0.24
C20:4
0.81 0.45 0.67 0.41 0.00 0.00 0.00 0.00 n-7
C20:4
7.22 12.23 6.84 12.18 1.19 2.26 1 .31 2.32 n-6
C22: l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
C20:4
0.63 0.52 0.00 0.46 0.00 0.00 0.00 0.00 n-5
C20:4
3.45 5.45 3.33 5.58 0.00 2.40 0.00 2.34 n-3
C20:3
0.09 0.00 0. 1 1 0.00 0.00 0.00 0.00 0.00 n-3
C20:5
107.31 186.83 92.99 169.32 40.32 90.08 43.15 92.54 n-3
C22:4
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
C24:0 0.60 0.00 0.52 0.00 2.81 6.83 2.74 6.53
C24: l
1 .55 3.26 0.85 2.04 0.43 1.34 0.42 1.24 n-9
C22:5
9.66 15.84 10.27 17.98 2.42 4.68 2.32 4.21 n-6
C22:5
20.44 35.13 9.92 17.50 2.41 4.94 2.69 5.23 n-3
C22:6
246.98 423.10 245.96 444.08 139.58 289.34 137.35 277.57 n-3
Sum
of 527.15 907.18 518.71 942.75 367.89 805.29 372.63 799.68 FAME
Table 5 : Fatty Acid Profiles of PTA- 10208 and PTA- 10212 Biomasses and
Extracted Crude Lipids (%)
PTA- PTA- PTA- PTA- PTA- PTA- PTA- PTA- 10208 10208 10208 10208 10212 10212 10212 10212 Sample Sample Sample Sample Sample Sample Sample Sample # 1 #1 #2 #2 #1 #1 #2 #2
Crude Crude Crude Crude
Biomass Lipid Biomass Lipid Biomass Lipid Biomass Lipid
Fatty %
% FAME % FAME % FAME % FAME % FAME % FAME % FAME Acid FAME
C12:0 0.28 0.27 0.35 0.33 0.27 0.24 0.23 0.24
C14:0 2.20 2.22 3.22 3.29 1.50 1.60 1.60 1.71
C14: l 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
C15:0 0.46 0.41 0.69 0.66 2.48 2.54 2.52 2.60
C16:0 19.93 20.1 1 22.70 23.07 39.65 40.79 39.68 40.93 PTA- PTA- PTA- PTA- PTA- PTA- PTA- PTA- 10208 10208 10208 10208 10212 10212 10212 10212 Sample Sample Sample Sample Sample Sample Sample Sample #1 #1 #2 #2 # 1 #1 #2 #2
Crude Crude Crude Crude
Biomass Lipid Biomass Lipid Biomass Lipid Biomass Lipid
C16: l 0.00 0.00 0.01 0.00 1.70 1.80 2.00 2.1 1
C1 8:0 1 .02 0.99 0.92 0.89 1 .84 1.91 1 .82 1.89
C18: l
0.00 0.36 0.00 0.33 0.01 0.50 0.02 0.73 n-9
CI S: 1
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-7
C18:2
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C20:0 0.28 0.20 0.27 0.20 0.43 0.38 0.45 0.40
C18:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-3
C20: l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
CI 8:4
0.17 0.18 0.21 0.21 0.62 0.32 0.59 0.33 n-3
C20:2
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C20:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C22:0 0.02 0.00 0.01 0.00 0.08 0.02 0.09 0.03
C20:4
0.15 0.05 0.13 0.04 0.00 0.00 0.00 0.00 n-7
C20:4
1 .37 1 .35 1.32 1.29 0.32 0.28 0.35 0.29 n-6
C22: l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
C20:4
0.12 0.06 0.00 0.05 0.00 0.00 0.00 0.00 n-5
C20:4
0.65 0.60 0.64 0.59 0.00 0.30 0.00 0.29 n-3
C20:3
0.02 0.00 0.02 0.00 0.00 0.00 0.00 0.00 n-3
C20:5
20.36 20.59 17.93 17.96 10.96 1 1.19 1 1 .58 1 1.57 n-3
C22:4
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
C24:0 0.1 1 0.00 0.10 0.00 0.76 0.85 0.74 0.82
C24: l
0.29 0.36 0.16 0.22 0.12 0.17 0.1 1 0.16 n-9
C22:5
1.83 1.75 1.98 1.91 0.66 0.58 0.62 0.53 n-6
C22:5
3.88 3.87 1.91 1.86 0.65 0.61 0.72 0.65 n-3
C22:6
46.85 46.64 47.42 47.10 37.94 35.93 36.86 34.71 n-3
Sum
of
100 100 100 100 100 100 100 100 FAME
% Table 6: Fatty Acid Profiles of PTA- 10208 and PTA-10212 Isolated TAG
PTA- PTA- PTA- PTA- PTA- PTA- PTA- PTA- 10208 10208 10208 10208 10212 10212 10212 10212 Sample Sample Sample Sample Sample Sample Sample Sample
#1 #1 #2 #2 #1 #1 #2 #2
Fatty FAME % FAME FAME % FAME
% FAME % FAME Acid (mg/g) FAME (mg/g) (mg/g) FAME (mg/g)
C12:0 2.57 0.27 3.35 0.36 0.00 0.00 0.00 0.00
C14:0 21.07 2.23 31.37 3.41 14.05 1.61 14.45 1.69
C14:l 0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00
C15:0 3.89 0.41 6.17 0.67 23.27 2.66 23.14 2.71
C16:0 189.28 20.07 218.78 23.75 399.51 45.75 402.43 47.07
C16:l 0.00 0.00 0.00 0.00 15.23 1.74 17.62 2.06
C18:0 9.21 0.98 8.07 0.88 22.70 2.60 23.10 2.70
C18:l
3.35 0.36 3.64 0.40 6.12 0.70 7.48 0.87 n-9
C18:l
0.00 0.00 0.00 0.00 <0.1 <0.1 <0.1 <0.1 n-7
CI 8:2
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C20:0 1.86 0.20 1.55 0.17 4.76 0.55 5.32 0.62
C18:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-3
C20:l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
CI 8:4
1.64 0.17 2.00 0.22 2.25 0.26 2.24 0.26 n-3
C20:2
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C20:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-6
C22:0 0.00 0.00 0.00 0.00 0.55 0.06 0.89 0.10
Un¬
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 known
C20:4
0.39 0.04 0.05 0.01 0.00 0.00 0.00 0.00 n-7
C20:3
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-3
C20:4
12.79 1.36 11.82 1.28 2.33 0.27 2.25 0.26 n-6
C22:l
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
C20:4
0.39 0.04 0.07 0.01 0.00 0.00 0.00 0.00 n-5
C20:4
5.52 0.59 5.09 0.55 2.87 0.33 2.98 0.35 n-3
C20:5
197.14 20.90 166.68 18.10 91.17 10.44 91.78 10.74 n-3
C24:0 0.00 0.00 0.00 0.00 6.93 0.79 7.36 0.86
C22:4
0.00 0.00 0.00 0.00 0.00 0.00 0.00 0.00 n-9
C24:l
1.08 0.11 <0.1 <0.1 0.00 0.00 0.00 0.00 n-9
C22:5
15.88 1.68 16.57 1.80 4.01 0.46 3.39 0.40 n-6
C22:5
36.05 3.82 16.00 1.74 4.53 0.52 5.07 0.59 n-3 PTA- PTA- PTA- PTA- PTA- PTA- PTA- PTA- 10208 10208 10208 10208 10212 10212 10212 10212 Sample Sample Sample Sample Sample Sample Sample Sample #1 #1 #2 #2 #1 #1 #2 #2
C22:6
440.99 46.76 429.83 46.67 273.02 3 1.26 245.38 28.70 n-3
Sum
of 943. 1 1 - 921.03 - 873.31 - 854.89 - FAME
Total
% - 100.00 - 100.00 - 100.00 - 100.00 FAME
Table 7: Fatty Acid Profiles of PTA- 10212 Isolated PL
Figure imgf000060_0001
PTA-10212 Sample #3
The lipid content of the biomass for PTA-10212 Sample #3 was estimated to be
34% as the sum of FAME, and the amount of crude oil obtained after solvent extraction was 37% by weight, giving a 109% recovery of fat present in the biomass. After fractionation using flash chromatography, approximately 46% of the crude oil was isolated as TAG, 28%o was isolated as DAG, The crude oil contained 309 mg/g DHA and 264 mg/g EPA. The isolated TAG contained 341 mg/g DHA and 274 mg/g EPA. The isolated DAG fraction contained 262 mg/g DHA and 237 mg/g EPA. The total fatty acid profiles of the biomass, extracted crude oil, and isolated fractions are shown below in Table 8 and Table 9 calculated as mg/g and % FAME, respectively.
Table 8: Fatly Acid Profiles of PTA-10212 Sample #3 Biomass and Extracted Crude Lipid (mg/g)
Crude
Biomass TAG DAG
Oil
Wt. % NA 37.2% 46.0% 27.9%
FAME FAME FAME FAME
Fatty Acid
(mg/g) (mg/g) (mg/g) (mg/g)
C12:0 0.0 0.0 0.0 0.0
CI 4:0 3.6 10.3 1 1.5 9.4
C14: l 0.0 0.0 0.0 0.0
C15:0 4.1 10.6 9.8 6.6
C 16:0 70.5 181.8 231.7 1 1 1.3
C16: l 6.7 19.1 1 8.7 17.1
C 18:0 2.4 10.2 14.2 0.0
CI 8: 1 n-9 0.0 6.7 0.0 0.0
CI 8: 1 n-7 0.0 1.2 0.0 0.0
C18:2 n-6 0.0 1.8 0.0 0.0
C20:0 0.0 2.4 0.0 0.0
C18:3 n-3 0.0 0.0 0.0 0.0
C20: l n-9 0.0 0.3 0.0 1.7
C18:4 n-3 1.9 3.4 3.2 4.4
C20:2 n-6 0.0 0.0 0.0 0.0
C20:3 n-6 0.0 0.0 0.0 0.0
C22:0 3.3 0.0 0.0 0.0
C20:4 n-7 0.0 2.1 1.5 0.0
C20:3 n-3 0.0 0.0 0.0 0.0
C20:4 n-6 6.8 17.9 21.4 13.8
C22: l n-9 0.0 0.0 0.0 0.0
C20:4 n-5 0.0 1.3 1.3 0.0 Crude
Biomass TAG DAG
Oil
C20:4 n-3 3.0 8.5 10.9 6.4
C20:5 n-3 102.0 263.6 274.2 237.4
C24:0 0.0 1.7 3.9 0.0
C22:4 n-9 0.0 0.0 0.0 0.0
C24: l n-9 0.0 0.0 4.2 0.0
C22:5 n-6 3.2 8.3 10.7 6.1
C22:5 n-3 3.8 10.4 15.1 6.6
C22:6 n-3 13 1.2 309.4 341.1 261.9
Sum of
342.4 871.1 973.2 682.6
FAME
Table 9: Fatty Acid Profiles of PTA-10212 Sample #3 Biomass and Extracted Crude Lipid (%)
Biomass Crude Oil TAG DAG
Wt. % NA 37.2% 46.0% 27.9%
Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
C12:0 0.0 0.0 0.0 0.0
C 14:0 1.1 1 .2 1.2 1.4
C14: l 0.0 0.0 0.0 0.0
C15:0 1.2 1.2 1.0 1.0
C16:0 20.6 20.9 23.8 16.3
C16: l 2.0 2.2 1.9 2.5
C 18:0 0.7 1 .2 1.5 0.0
C I 8: 1 n-9 0.0 0.8 0.0 0.0
C18: l n-7 0.0 0.1 0.0 0.0
CI 8:2 n-6 0.0 0.2 0.0 0.0
C20:0 0.0 0.3 0.0 0.0
C18:3 n-3 0.0 0.0 0.0 0.0
C20: l n-9 0.0 0.0 0.0 0.2
CI 8:4 n-3 0.6 0.4 0.3 0.6
C20:2 n-6 0.0 0.0 0.0 0.0
C20:3 n-6 0.0 0.0 0.0 0.0
C22:0 1.0 0.0 0.0 0.0
C20:4 n-7 0.0 0.2 0.2 0.0
C20:3 n-3 0.0 0.0 0.0 0.0
C20:4 n-6 2.0 2.1 2.2 2.0
C22: l n-9 0.0 0.0 0.0 0.0
C20:4 n-5 0.0 0.1 0.1 0.0
C20:4 n-3 0.9 1.0 1.1 0.9
C20:5 n-3 29.8 30.3 28.2 34.8
C24:0 0.0 0.2 0.4 0.0
C22:4 n-9 0.0 0.0 0.0 0.0 Biomass Crude Oil TAG DAG
C24: l n-9 0.0 0.0 0.4 0.0
C22:5 n-6 0.9 1 .0 1.1 0.9
C22:5 n-3 1 . 1 1.2 1.6 1.0
C22:6 n-3 38.3 35.5 35.1 38.4
Total % FAME 100.0 100.0 100.0 100.0
P I A- 10212 Sample #4
PTA-10212 Sample #4 contained approximately 23% lipid determined as the sum of FAME, of which 107% was recovered using hexane extraction. After fractionation using flash chromatography, approximately 42% of the crude oil was isolated as TAG, 18% was isolated as DAG. The crude oil contained 275 mg/g DHA and 209 mg/g EPA. The isolated TAG contained 296 mg/g DHA and 205 mg/g EPA. The isolated DAG fraction contained 245 mg/g DHA and 219 mg/g EPA. The total fatty acid profiles of the biomass, extracted crude oil, and isolated fractions are shown below in Table 10 (mg/g) and Table 1 1 (%FAME).
Table 10: Fatty Acid Profiles of PTA-10212 Sample #4 Biomass and Extracted Crude Lipid (mg/g)
Biomass Crude Oil TAG DAG
Wt. % NA 24.7% 42.2% 1 8.4%
Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
C12:0 0.0 0.0 2. 1 2.4
C14:0 2.0 8.3 9.8 9.6
C14: l 0.0 0.0 0.0 0.0
C15:0 4.8 16.8 0.4 0.9
C16:0 63.3 210.6 285.7 138.0
C16: l 1.6 6.7 7.4 7.5
C 18:0 2.8 12.2 19.9 4.6
CI S: 1 n-9 0.0 3.7 0.7 1.1
C 18: l n-7 0.0 0.0 0.3 1.2
CI 8:2 n-6 0.0 0.0 0.0 0.0
C20:0 0.0 3.3 6.0 1.5
C18:3 n-3 0.0 0.0 0.0 0.0
C20: l n-9 0.0 0.0 0.7 1 .2
C 1 8:4 n-3 1.4 3.8 3.6 5.0
C20:2 n-6 0.0 0.0 0.0 0.0
C20:3 n-6 0.0 0.0 0.4 0.0
C22:0 1.5 0.0 1.9 0.0
C20:4 n-7 0.0 0.0 0.9 0.6 Biomass Crude Oil TAG DAG
C20:3 n-3 0.0 0.0 0.0 0.0
C20:4 n-6 2.5 10.1 13.0 10.3
C22: l n-9 0.0 0.0 0.0 0.0
C20:4 n-5 0.0 0.0 0.8 0.7
C20:4 n-3 1.4 6.3 8.6 6.0
C20:5 n-3 57.6 209. 1 205.4 219.0
C24:0 0.0 2.6 0.8 0.0
C22:4 n-9 0. 1 0.0 0.0 0.0
C24: l n-9 0.0 0.0 1 . 1 0.5
C22:5 n-6 1 .4 6.1 7.9 4.5
C22:5 n-3 4.0 15.8 20.8 12.9
C22:6 n-3 87.7 275.0 296.4 244.8
Sum of FAME 232.2 790.1 894.8 672.4
Table 1 1 : Fatty Acid Profiles of PTA- 10212 Sample #4 Biomass and Extracted Crude Lipid (%)
Biomass Crude Oil TAG DAG
wt. % NA 24.7% 42.2% 18.4%
Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g) FAME (mg/g)
C12:0 0.0 0.0 0.2 0.4
C14:0 0.9 1.0 1.1 1 .4
C14: l 0.0 0.0 0.0 0.0
C15:0 2.1 2.1 0.0 0.1
C16:0 27.3 26.7 3 1.9 20.5
C16: l 0.7 0.8 0.8 1.1
C18:0 1.2 1 .5 2.2 0.7
C18: l n-9 0.0 0.5 0.1 0.2
C18: l n-7 0.0 0.0 0.0 0.2
C18:2 n-6 0.0 0.0 0.0 0.0
C20:0 0.0 0.4 0.7 0.2
C18:3 n-3 0.0 0.0 0.0 0.0
C20: l n-9 0.0 0.0 0.1 0.2
C18:4 n-3 0.6 0.5 0.4 0.7
C20:2 n-6 0.0 0.0 0.0 0.0
C20:3 n-6 0.0 0.0 0.0 0.0
C22:0 0.6 0.0 0.2 0.0
C20:4 n-7 0.0 0.0 0.1 0.1
C20:3 n-3 0.0 0.0 0.0 0.0
C20:4 n-6 1.1 1.3 1 .5 1.5
C22: l n-9 0.0 0.0 0.0 0.0
C20:4 n-5 0.0 0.0 0.1 0.1 Biomass Crude Oil TAG DAG
C20:4 n-3 0.6 0.8 1 .0 0.9
C20:5 n-3 24.8 26.5 23.0 32.6
C24:0 0.0 0.3 0.1 0.0
C22:4 n-9 0.0 0.0 0.0 0.0
C24: l n-9 0.0 0.0 0.1 0.1
C22:5 n-6 0.6 0.8 0.9 0.7
C22:5 n-3 1.7 2.0 2.3 1.9
C22:6 n-3 37.8 34.8 33.1 36.4
Total % FAME 100.0 100.0 100.0 100.0
PTA-10212 Sample #5
[0162] A sample of crude oil was extracted from a biomass of PTA-10212 using the
FRIOLEX® process (GEA Westfalia Separator UK Ltd., Milton Keynes, England) to yield microbial oil PTA-10212 Sample #5. Individual lipid classes were isolated from PTA-10212 Sample #5 using low pressure flash chromatography, and the weight percent of each class was determined. The fatty acid profile of each class was determined using GC-FID.
1016 1 Briefly, the sample was prepared by dissolving 240 mg of crude oil in 600 μΐ, of hexane and applying to the head of the column. After fractionation of the sample using flash chromatography, the combined weights of all the fractions was 240 mg giving a 100% recovery. The sterol ester fraction accounted for 0.9%, the TAG fraction accounted for 42.6%., the free fatty acid (FFA) fraction accounted for 1.3%, the sterol fraction accounted for 2.2%, the DAG fraction accounted for 41.6%. The total fatty acid profiles of the FRIOLEX® crude oil and isolated fractions are shown below in Table 12 and Table 13 calculated as mg/g and % FAME, respectively.
Table 12: Fatty Acid Profiles of PTA-10212 Sample #5 Crude Oil (mg/g)
Crude Oil TAG DAG
Wt. % NA 42.6% 41.6%
Fatty Acid FAME (mg/g) FAME (mg/g) FAME (mg/g)
C12:0 0 0.7 1 .0
C 14:0 7.7 7.7 8.5
C 14: l 0 0.0 0.0
C15:0 10.3 1 1.7 9.3
C16:0 179.3 217.7 134.6
C16: l 18. 1 16.3 25.9
C18:0 8.1 13.2 2.3
CI 8: 1 n-9 4.7 8.4 0.7
C18: l n-7 0 1.8 1.0
C I 8:2 n-6 1 .8 3.3 0.7
C20:0 1.9 3.6 0.2
C 18:3 n-3 0 0.0 0.0
C20: l n-9 0 0.7 1.0
CI 8:4 n-3 3.1 2.8 3.8
C20:2 n-6 0 0.0 0.0
C20:3 n-6 0 0.6 0.4
C22:0 0 1.5 0.0
C20:4 n-7 0 1.0 0.7
C20:3 n-3 0 0.0 0.0
C20:4 n-6 12.7 16.1 13.6
C22: l n-9 0 0.0 0.0
C20:4 n-5 0 1.5 0.8
C20:4 n-3 6.5 9.3 6.4
C20:5 n-3 213.3 223.7 252.8
C24:0 2.3 4.4 0.6
C22:4 n-9 0 1.9 0.9
C24: l n-9 0 0.0 0.0
C22:5 n-6 7.9 9.5 8.3
C22:5 n-3 13 20.6 9.7
C22:6 n-3 305.6 327.4 353.8
Sum of FAME 796.6 905.3 837.4 Table 13: Fatty Acid Profiles of PTA-10212 Sample #5 Crude Oil (%)
Crude Oil TAG DAG
Fatty Acid % FAME % FAME % FAME
C12:0 0 0.1 0.1
C14:0 1 0.9 1.0
C14:l 0 0.0 0.0
C15:0 1.3 1.3 1.1
C16:0 22.5 24.0 16.1
C16:l 2.3 1.8 3.1
C18:0 1 1.5 0.3
C18:l n-9 0.6 0.9 0.1
C18:l n-7 0 0.2 0.1
C18:2n-6 0.2 0.4 0.1
C20:0 0.2 0.4 0.0
C18:3 n-3 0 0.0 0.0
C20:l n-9 0 0.1 0.1
CI 8:4 n-3 0.4 0.3 0.5
C20:2 n-6 0 0.0 0.0
C20:3 n-6 0 0.1 0.0
C22:0 0 0.2 0.0
C20:4 n-7 0 0.1 0.1
C20:3 n-3 0 0.0 0.0
C20:4 n-6 1.6 1.8 1.6
C22:l n-9 0 0.0 0.0
C20:4 n-5 0 0.2 0.1
C20:4 n-3 0.8 1.0 0.8
C20:5 n-3 26.8 24.7 30.2
C24:0 0.3 0.5 0.1
C22:4 n-9 0 0.2 0.1
C24:l n-9 0 0.0 0.0
C22:5 n-6 1 1.1 1.0
C22:5 n-3 1.6 2.3 1.2
C22:6 n-3 38.4 36.2 42.3
Total % FAME 100 100 100 EXAMPLE 4
[0164] The relative amount and fatty acid composition of each TAG isomer present in the extracted crude lipid was determined for each of samples PTA- 10208 Sample #1, PTA- 10208 Sample #2, PTA-10212 Sample #1 , PTA-10212 Sample #2, and PTA-10212 Sample #3, PTA-10212 Sample #4, and PTA-10212 Sample #5 from Example 3 using non-aqueous reversed phase HPLC separation and APCI-MS detection.
[0165] TAG Method -
Instrument Agilent 1 100 HPLC
Agilent 1 100 MSD
Column(s) Two Phenomenex Luna CI 8 (2), 150 x 4.6 mm,
3 μιη particle size connected in series
Mobile Phase A - Acetonitrile
B - IP A w/ 0.1% Ammonium Acetate
Gradient
Figure imgf000068_0001
Column Temp. 20°C
Flow Rate 0.5 mL/min
Injection Volume 5 xL
MSD Mass Range 350 - 1150
Fragmentor 225 V
Drying Gas Temperature 350°C,
Vaporizor Temperature 325°C
Capillary Voltage 3500 V
Corona Current 10 μΑ
PTA- 10208 Sample #1
[0166] The crude lipid isolated from PTA- 10208 Sample #1 was prepared for TAG analysis prepared for TAG analysis by weighing 5.5 mg of oil into an HPLC vial and diluting with 1 ml , of hexane. Table 14: Identification of TAG Species in PTA- 10208 Sample #1
Figure imgf000069_0001
PTA-10208 Sample #2
The crude lipid isolated from PTA-10208 Sample #2 was prepared for TAG analysis prepared for TAG analysis by weighing 5.3 mg of oil into an HPLC vial and diluting with 1 niL of hexane. Table 15: Identification of TAG Species in PTA- 10208 Sample #2
Figure imgf000070_0001
PTA-10212 Sample #1
The crude lipid isolated from PTA- 10212 Sample #1 was prepared for TAG analysis prepared for TAG analysis by weighing 5.3 mg of oil into an HPLC vial and diluting with 1 mL of hexane. Table 16: Identification of TAG Species in PTA-10212 Sample #1
Figure imgf000071_0001
ND= Not Detected PTA-10212 Sample #2
The crade lipid isolated from PTA-10212 Sample #2 was prepared for TAG analysis prepared for TAG analysis by weighing 3.6 mg of oil into an HPLC vial and diluting with 1 mL of hexane.
Table 17: Identification of TAG Species in PTA-10212 Sample #2
Figure imgf000072_0001
ND= Not Detected PTA-10212 Sample #3
A sample of the TAG fraction of PTA-10212 Sample #3 was prepared in hexane and analyzed by HPLC/APCl/MS to determine the identities of individual TAG isomers.
Table 1 8: Identification of TAG Species in PTA- 10212 Sample #3
Figure imgf000073_0001
ND= Not Detected PTA-10212 Sample #4
A sample of the TAG fraction of PTA-10212 Sample #4 was prepared in hexane and analyzed by HPLC/APCI/MS to determine the identities of individual TAG isomers.
19: Identification of TAG Species in PTA- 10212 Sample #4
Figure imgf000074_0001
ND= Not Detected PTA-10212 Sample #5
A sample of the TAG fraction of PTA-10212 Sample #5 was prepared in hexane and analyzed by HPLC/APCI/MS to determine the identities of individual TAG isomers. Table 20: Identification of TAG Species in PTA- 10212 Sample #5
Retention Peak Identification Area
[M + H] + [Μ + ΝΗ4 (DAG) Fragments Time # Percent
21.0 1 EPA/EPA/EPA 1.7 945.7 962.8 643.5
21 .5 2 EPA/EPA/DHA 5.5 971.6 988.7 643.5 ,669.5
22.0 3 DHA/DHA/EPA 7.6 997.7 1014.7 695.5, 669.5
22.5 4 DHA/DHA/DHA 4.5 1023.8 1040.7 695.5
23.0 5 EPA/EPA/DPA 0.5 973.8 990.8 645.5, 671.5
DHA/EPA/DPA 999.7 1016.7 697.5, 671.5
23.3 6 1.5
EPA/ EPA /ARA 947.6 964.8 645.5
EPA/ARA/DHA 973.6 990.7 671.5, 645.4
23.7 7 1.9
DHA/DPA/DHA 1025.7 1042.7 695.5, 697.5
24.2 8 DHA/EPA/DPA 1.1 999.7 1016.7 669.5, 671.4, 696.5
DHA/DHA/DPA 1025.7 1042.9 695.5, 697.5
24.8 9 0.6
DHA 14:0/EPA 897.7 914.7 595.5
25.3 10 DHA/16: 1/EPA 0.7 923.8 940.8 595.5, 621.3
25.6 1 1 DHA/14:0/EPA 0.6 897.7 914.7 569.3, 595.4
25.8 12 DHA/16: 1/ DHA 0.5 949.7 966.7 621.3, 695.5
26.0 13 DHA/16: 1/EPA 0.4 923.7 940.8 595.5, 621.3
26.9 14 EPA/15:0/DHA 0.7 91 1.7 928.7 583.5, 609.3
27.4 15 DHA/15:0/DHA 0.7 937.6 954.8 609.3
27.8 16 EPA/16:0/EPA 4.9 899.7 916.7 597.5
28.2 17 EPA/16:0/DHA 14.3 925.7 942.8 597.5, 623.5
28.7 18 DHA/16:0/DHA 12.2 951.7 968.8 623.5
29.3 19 DPA/14:0/ARA 0.6 901.7 918.8 597.3
29.5 20 EPA/1 8:0/EPA 1 .5 927.7 944.8 625.5
30.0 21 DHA/16:0/ARA 3.4 953.7 970.8 623.4
30.6 22 EPA/EPA/18:0 2.1 927.7 944.7 599.5, 625.5, 669.3
31 .0 23 DHA/18:0/EPA 1.7 953.8 970.8 625.4, 651.5
3 1.3 24 DHA/18:0/DHA 0.9 979.7 996.8 651.5, 695.3
31.9 26 16:0/DHA/14:0 0.8 851.7 868.7 595.5, 623.5
32.3 27 18: 1/14:0/DHA 1.7 877.7 894.7 549.5, 595.5
32.6 28 DHA/16:0/14:0 0.9 851.8 868.7 523.4, 623.5
EPA/15:0/16:0 839.7 856.7 537.5, 583.3
33.5 29 0.7
DHA/20:0/EPA 981.7 998.8 653.5, 679.6
33.9 30 DHA/16:0/15:0 1.2 865.7 882.7 537.5, 623.5
34.8 3 1 EPA/16:0/16:0 3.9 853.8 870.7 551.5, 597.5
35.2 32 DHA/16:0/16:0 10.6 879.7 896.7 551.5, 623.5
36.4 33 DP A/16:0/16:0 1.5 881.7 898.7 551.5, 625.5
37.4 33 DPA/16:0/16:0 1 .2 881.7 898.7 551.5, 625.5
37.7 34 DHA/16:0/18:0 1.9 907.7 924.7 579.4
38.4 35 EPA/24: 0/DH A 0.5 1037.8 1054.8 709.5, 735.6
38.8 36 DHA/24:0/DHA 1.0 1064.8 1081.8 735.7 EXAMPLE 5
[0173] Crude oils were further processed via refining, bleaching, and deodorizing to obtain refined oils. The refined oils were diluted with high oleic sunflower oil to obtain final oils with a DHA content of approximately 400 mg/g. Individual lipid classes were isolated and the fatty acid profiles of each class was determined using GC-FID as FAME.
PTA-1 G208 Final Oils
[0174] The fatty acid profiles for PTA-10208 Final Oils #1-5 are summarized in Tables
21-22, including profiles associated within the isolated TAG fraction (Tables 23-24) and the isolated sterols/DAG fraction (Tables 24-26).
[0175] Individual lipid classes in the final oils were also determined using flash chromatography (Table 27) and normal HPLC with ELSD and APCI-MS confirmation
(Table 28).
Table 21 : Fatty Acid Profiles of PTA- 10208 Final Oils (mg/g)
Figure imgf000077_0001
Table 22: Fatty Acid Profiles of PTA- 10208 Final Oils (%)
PTA- 10208 PTA- 10208 PTA- 10208 PTA- 10208 PTA- 10208 Final Oil #1 Final Oil #2 Final Oil #3 Final Oil #4 Final Oil #5
Fatty Acid % FAME % FAME % FAME % FAME % FAME
C12:0 0.3 0.3 0.3 0.3 0.3
C 14:0 1 .8 1 .6 2.3 2.0 1.9
C14: l 0.0 0.0 0.0 0.0 0.0
C 15:0 0.4 0.4 0.5 0.4 0.4
C16:0 20.9 19.2 21.1 19.9 21.3
C 16: l <0.1 <0.1 <0.1 <0.1 0. 1
C17:0 0. 1 0.1 0.1 0. 1 0.2
C 18:0 1.4 1.5 1.3 1.3 1.4
C18: l n-9 2.6 8.8 2.8 2.8 3.2
C I S: 1 n-7 <0.1 0.1 <0.1 <0.1 <0. 1
C18:2 n-6 0.4 0.9 0.4 0.4 0.5
C20:0 0.5 0.4 0.4 0.4 0.4
CI 8:3 n-3 0.0 0.0 0.0 0.0 0.0
C20: l n-9 <0.1 <0.1 <0.1 <0.1 <0.1
CI 8:4 n-3 0.3 0.3 0.3 0.3 0.3
C20:2 n-6 0.0 0.0 0.0 0.0 0.0
C20:3 n-6 <0.1 <0.1 <0.1 <0.1 <0.1
C22:0 0.1 0.2 0.1 0.1 0. 1
C20:4 n-7 0.2 0.2 0.2 0.2 0.2
C20:3 n-3 0.0 0.0 0.0 0.0 0.0
C20:4 n-6 1 .4 1.3 1.5 1.5 1 .5
C22: l n-9 0.0 0.0 0.0 0.0 0.0
C20:4 \n-5 0.2 0.2 0.2 0.2 0.2
C20:4 \n-3 0.7 0.6 0.7 0.7 0.7
C20:5 n-3 18.9 17.5 21.5 22.7 21.6
C24:0 0.1 0.2 0.1 0.1 0.1
C22:4 n-9 0.0 0.0 0.0 0.0 0.0
C24: l n-9 0.4 0.3 0.2 0.3 0.2
C22:5 n-6 1.6 1.5 1.6 1.4 1.4
C22:5 n-3 4.8 4.4 3.6 4.4 4.0
C22:6 n-3 43.0 40.1 40.8 40.5 39.9 Table 23 : Isolated TAG Fatty Acid Profiles: PTA- 10208 Final Oils (mg/g)
Figure imgf000079_0001
Table 24: Isolated TAG Fatty Acid Profiles: PTA-10208 Final Oils (%)
PTA- 10208 PTA- 10208 PTA-10208 PTA-10208 PTA-10208 Final Oil #1 Final Oil #2 Final Oil #3 Final Oil #4 Final Oil #5
Fatty Acid % FAME % FAME % FAME % FAME % FAME
C12:0 0.3 0.2 0.3 0.3 0.3
C14:0 1.8 1.6 0.3 0.3 0.3
C14:l 0.0 0.0 0.0 0.0 0.0
C15:0 0.4 0.4 0.5 0.4 0.4
C16:0 20.9 19.2 21.2 20.0 21.2
C16:l <0.1 <0.1 0.1 0.1 0.1
C17:0 0.1 0.1 0.1 0.1 0.1
C18:0 1.4 1.5 1.3 1.3 1.4
CI 8:1 n-9 2.6 8.9 2.9 2.8 3.6
CI 8:1 n-7 <0.1 0.1 <0.1 <0.1 <0.1
CI 8:2 n-6 0.3 0.8 0.4 0.4 0.4
C20:0 0.5 0.4 0.4 0.4 0.4
CI 8:3 n-3 0.0 0.0 0.0 0.0 0.0
C20:l n-9 <0.1 <0.1 <0.1 <0.1 <0.1
CI 8:4 n-3 0.3 0.3 0.3 0.3 0.3
C20:2 n-6 0.0 0.0 0.0 0.0 0.0
C20:3 n-6 <0.1 <0.1 <0.1 <0.1 <0.1
C22:0 0.1 0.2 0.1 0.1 0.1
C20:4 n-7 0.2 0.2 0.2 0.2 0.2
C20:3 n-3 0.0 0.0 0.0 0.0 0.0
C20:4 n-6 1.4 1.3 1.5 1.5 1.5
C22:l n-9 0.0 0.0 0.0 0.0 0.0
C20:4 n-5 0.2 0.2 0.2 0.2 0.2
C20:4 n-3 0.7 0.6 0.7 0.6 0.7
C20:5 n-3 19.0 17.6 21.5 22.7 21.6
C24:0 0.1 0.1 0.1 0.1 0.1
C22:4 n-9 0.0 0.0 0.0 0.0 0.0
C24:l n-9 0.4 0.3 0.2 0.3 0.3
C22:5 n-6 1.6 1.5 1.6 1.4 1.4
C22:5 n-3 4.8 4.4 3.6 4.4 4.1
C22:6 n-3 42.9 40.0 40.7 40.4 39.8 Table 25: Isolated Sterols/DAG Fatty Acid Profiles: PTA- 10208 Final Oils
(mg/g)
Figure imgf000081_0001
Table 26: Isolated Sterols/DAG Fatty Acid Profiles: PTA- 10208 Final Oils (%)
PTA- 10208 PTA- 10208 PTA- 10208 PTA- 10208 PTA- 10208
Final Oil #1 Final Oil #2 Final Oil #3 Final Oil #4 Final Oil #5
Fatty Acid % FAME % FAME % FAME % FAME % FAME
C12:0 0.3 0.3 0.5 0.4 0.4
C14.0 1.7 1.5 1.8 1.8 1.6
C14: l 0.0 0.0 0.0 0.0 0.0
C15:0 0.4 0.4 0.4 0.4 0.4
C16:0 23.3 20.8 19.9 20.5 21.8
C16: l <0.1 <0.1 <0.1 <0.1 0.1
C17:0 0.0 0.0 0.1 0. 1 0.1
C18:0 1.3 1.3 1.2 1.2 1.2
CI 8: 1 n-9 2.6 8.9 8.6 3.3 6.2
CI 8: 1 n-7 0.1 0.1 <0.1 <0. 1 <0.1
C I 8:2 n-6 2.3 2.7 3.9 2.4 3.8
C20:0 0.4 0.3 0.2 0.3 0.3
C18:3 n-3 0.0 0.0 0.0 0.0 0.0
C20: l n-9 <0.1 <0.1 <0.1 <0.1 <0.1
CI 8:4 n-3 0.4 0.4 0.4 0.4 0.4
C20:2 n-6 0.0 0.0 0.0 0.0 0.0
C20:3 n-6 <0.1 <0.1 <0.1 <0.1 <0.1
C22:0 0.1 0.2 0. 1 0.1 0.1
C20:4 n-7 0.1 0.1 0.4 0.2 0.1
C20:3 n-3 0.0 0.0 0.0 0.0 0.0
C20:4 n-6 1.0 0.9 0.9 1.1 0.9
C22: l n-9 0.0 0.0 0.0 0.0 0.0
C20:4 n-5 <0.1 <0.1 <0.1 0.1 <0.1
C20:4 n-3 0.5 0.4 0.4 0.5 0.4
C20:5 n-3 16.3 15.2 16.6 19.6 17.4
C24:0 0.2 0.2 0.2 0.2 0.3
C22:4 n-9 0.0 0.0 0.0 0.0 0.0
C24: l n-9 0.3 0.3 0.2 0.3 0.2
C22:5 n-6 1.4 1.3 1.2 1.2 1.1
C22:5 n-3 3.9 3.7 2.5 3.6 2.9
C22:6 n-3 43.3 40.8 40.5 42.3 40.2 Table 27: Lipid class separation by flash chromatography (wt %)
PTA- PTA-
PTA- 10208 PTA- 1 0208 PTA- 10208 10208 10208
Lipid Class Separation
Final Oil # 1 Final Oil #2 Final Oil #3 Final Oil Final Oil
#4 #5
TAG 93.4 95.4 94.0 95.7 95.1
Sterols/DAG 3.1 2.9 2.6 3.0 2.9
Recovery (%) 96.5 98.3 96.6 98.7 98.0
Table 28: Lipid class separation by HPLC-ELSD (wt %)
Figure imgf000083_0001
ND= Not Detected
PTA-10212 Final Oil
DHA was present in a PTA-10212 Final Oil at 41.63% and 366.9 mg/g, while EPA was present at 16.52%. Individual fatty acid profiles were determined and are summarized in Table 29.
Table 29: Fatty Acid Profiles of PTA-10212 Final Oil (% FAME)
Figure imgf000084_0001
ND= Not Detected EXAMPLE 6 An analysis of the triacylglycerides (TAGs) of the PTA- 10208 final oils described in Example 5 was performed using techniques described in Example 4. The identification of each fatty acid moiety was made, as summarized in Table 30 below.
Table 30: Identi fication of TAG Species in PTA- 10208 Final Oil
PTA- 10208 PTA- 10208 PTA- 10208 PTA- 10208 PTA- 10208
Identification
Final Oil #1 Final Oil #2 Final Oil #3 Final Oil #4 Final Oil #5
Area % Area % Area % Area % Area %
EPA/EPA/EPA 1 .3 1.0 1.9 1.7 1 .4
EPA/EPA/DHA 8.2 6.0 7.3 6.8 6.4
DHA/DHA/EPA 14.2 1 l . l 10.6 9.5 8.7
DHA/DHA/DHA 10.2 8.3 7.6 6.1 5.7
DPA/EP A/EPA 1.2 0.9 1.0 1.1 1.1
DHA/DPA/EPA 3.0 2.4 2.5 2.3 2.9
DHA/EPA/ARA 3.8 3.0 3.0 3.0 2.3
DHA/DPA/DHA
DHA/DPA/EPA 2.3 1.9 1.5 1.6 1.7
DHA/DPA/DHA 1.7 1.2 1.1 1.2 1.2
EPA/14:0/DHA 1.1 1.0 1.8 1.8 1.5
DHA/DHA/14:0 1.1 1.0 1.4 1.3 1.3
EPA/EPA/16:0 2.3 2.3 3.4 3.9 3.3
DHA/! 6:0/EPA 12.1 12.5 12.9 14.0 13.4
DHA/16:0/DHA 16.1 16.8 17.5 14.8 17.2
EPA/EPA/18:0 2.1 2.0 1.7 2.1 2.7
DHA/DPA/16:0 3.0 3.3 2.3 2.9 2.7
DHA/16:0/ARA 1.6 1.6 1.8 2.0 2.2
DHA/16:0/DPA 1 .3 2.1 1.4 1 .5 2.5
DHA/18:0/DHA 0.8 0.8 0.7 0.8 1.0
DHA/14:0/16:0 0.6 1.0 1.3 1.4 1.3
EPA/16:0/16:0 0.9 1.1 1.5 1.7 2.0
DHA/16:0/16:0 3.6 4.8 5.5 5.7 6.5
1 8:0/16:0/DHA 0.4 0.8 0.7 0.8 1.2
1 8: 1 /1 8: 1/18: 1 0.6 4.0 1.0 1.4 1 .6 EXAMPLE 7
[0178] A two-day old inoculum flask of the isolated microorganisms deposited under
ATCC Accession Nos. PTA- 10208 and 10212 was prepared as a carbon and nitrogen-fed culture in media according to Tables 1 and 2.
[0179] Mutagenesis was carried out according to following procedure:
[0180] A sterile T=2 day old flask, approximately 50 ml, was poured into a sterile 40 ml glass homogenizer. The culture received 50 plunges in the homogenizer. The culture was pipeted out and filtered through a sterile 50 micron mesh filter, which was placed in a 50 ml sterile tube (the mesh was used as a means of retaining the larger clumps of colonies while letting the smaller clusters and single cells pass through the 50 micron mesh.). The entire concentrated macerate was collected in a sterile 50 ml tube. The macerated culture was vortexed and dilutions at levels up to 1 :100 fold were made. The diluted macerate samples were vortexed prior to adding 200 μΐ of inoculum to a media agar plate, 100 x 15 mm, containing 4-5 glass beads (3 mm glass beads). Each plate was gently agitated in an effort to have the beads spread the inoculum evenly around the plate. Beads were dumped off of plates and plates were left to sit with covers on for approximately 5 minutes to dry. Lights in both the sterile hood and adjoining areas were turned off as the procedure was performed in dim light. There was minimal light available to be able to run the procedure but only indirect and dim.
[0181] Five replicate plates were placed on the floor of the XL crosslinker (Spectronics
Corporation, New York) with the lids off while the samples were irradiated. The crosslinker delivered power in terms of microjoules and a level was sought that achieved a 90%-95% Kill. Five replicate control plates were inoculated with un-mutagenized cells using the same protocol. These cell counts were used to calculate the % Kill. Once the irradiation was finished the plates were taken out, the lids were replaced, and the plates were wrapped in parafilm followed by a wrap in aluminum foil. It was imperative that the plates grew for the first week in the dark so that they were not able to repair the damaged genes.
[0182] Plates were placed in a 22.5°C room for about 10 days prior to counting the colonies. When final counts were made, individual colonies were picked with a sterile inoculating loop and re-streaked on new media plates. Each colony was plated on an individual plate. As plates grew dense a sample was taken, using a inoculating loop, and inoculated into a sterile 250 ml shake flask containing 50 ml of media. This flask was placed on a shaker at 200 rpm in a 22.5 °C room. On T=7 days the shake flask culture was harvested into a 50 ml sterile tube. The pH was taken and the sample was centrifuged to collect the biomass pellet. Each sample was rinsed and re-suspended in a 50:50 mixture of isopropyl alcohol and distilled water prior to being re-centrifuged. The collected pellet was freeze dried, weighed, and a FAME analysis was performed. The data in Tables 31 and 32 represents mutants produced with the above process from strains PTA- 10208 and PTA-10212, respectively.
Table 3 1 : PTA- 10208 Mutants
control Mutant 1 Mutant 2 Mutant 3
Fatty Acids PTA-10208 PTA-10209 PTA- 10210 PTA- 1021 1
% 08:0 0.00 0.00 0.00 0.00
% 09:0 0.00 0.00 0.00 0.00
% 10:0 0.00 0.00 0.00 0.00
% 1 1 :0 0.00 0.00 0.00 0.00
% 1 1 :1 0.00 0.00 0.00 0.00
% 12:0 0.1 1 0.10 0.22 0.19
% 12:1 0.00 0.00 0.00 0.00
% 13:0 0.19 0.19 0.15 0.16
% 13: 1 0.00 0.00 0.00 0.00
% 14:0 1 .94 1 .82 2.98 2.59
% 14:1 0.00 0.00 0.00 0.00
% 15:1 2.66 2.22 1 .76 1 .66
% 16:0 24.87 24.97 23.71 25.01
% 16:1 0.20 0.25 0.07 0.07
% 16:2 0.00 0.00 0.00 0.00
% 16:3 0.00 0.00 0.00 0.00
% 17:0 1 .49 1 .21 0.62 0.66
% 18:0 1 .13 1 .14 0.91 1 .01
% 18:1 n-9 0.07 0.07 0.06 0.06
% 18:1 n-7 0.00 0.00 0.00 0.00
% 18:2 0.00 0.00 0.00 0.00
% 18 3 n-6 0.00 0.00 0.05 0.04
% 18 3 n-3 0.09 0.08 0.17 0.14
% 18 4 n-3 0.00 0.00 0.00 0.00
% 20:0 0.31 0.33 0.24 0.30
% 20:1 n-9 0.00 0.04 0.00 0.00
% 20:2 0.00 0.00 0.05 0.00
% 20:3 n-9 0.00 0.00 0.00 0.00 control Mutant 1 Mutant 2 Mutant 3
Fatty Acids PTA-10208 PTA- 10209 PTA- 10210 PTA- 1021 1
% 20:3 n-6 0.12 0.13 0.08 0.04
% 20:3 n-3 0.42 0.42 0.08 0.06
% 20:4
ARA 0.68 0.67 1 .44 1 .1 1
% 20:5 n-3
EPA 6.56 6.47 1 1 .99 9.87
% 22:0 0.07 0.07 0.06 0.07
% 22:1 0.00 0.00 0.00 0.00
% 22:2 0.1 1 0.09 0.10 0.08
% 22:3 0.00 0.00 0.00 0.00
% 22:4 n-6 0.00 0.00 0.00 0.00
% 22:5 n-6 2.32 2.36 2.36 2.36
% 22:5 n-3 0.48 0.66 0.66 0.52
% 22:6 n-3
DHA 51 .58 52.27 48.17 49.35
% 24:0 0.00 0.00 0.00 0.00
% 24:1 0.00 0.00 0.00 0.00
% Fat 47.87 49.41 66.00 63.12
% Unknown 4.61 4.45 4.07 4.64
Table 32: PTA- 10212 Mutants
Control Mutant 1 Mutant 2 Mutant 3
Fatty Acids PTA-10212 PTA- 10213 PTA-10214 PTA- 0215
% 08:0 0.00 0.00 0.00 0.00
% 09:0 0.00 0.00 0.00 0.00
% 10:0 0.00 0.00 0.00 0.00
% 1 :0 0.00 0.00 0.00 0.00
% 1 1 :1 0.00 0.00 0.00 0.00
% 12:0 0.00 0.00 0.00 0.00
% 12:1 0.00 0.00 0.00 0.00
% 13:0 0.00 0.00 0.21 0.20
% 13:1 0.00 0.00 0.00 0.00
% 14:0 0.68 0.77 0.62 0.97
% 14: 1 0.00 0.00 0.00 0.00
% 15:1 0.00 0.00 0.00 0.00
% 16:0 17.36 19.94 15.27 23.61
% 16:1 1 .45 2.33 1.40 2.57
% 16:2 0.00 0.00 0.00 0.00
% 16:3 0.00 0.00 0.00 0.00
% 17:0 0.20 0.21 0.18 0.27
% 18:0 0.78 0.82 0.79 0.81
% 18: 1 n-9 0.00 0.00 0.00 0.00
% 18: 1 n-7 0.18 0.27 0.20 0.19 Control Mutant 1 Mutant 2 Mutant 3
Fatty Acids PTA-10212 PTA-10213 PTA-10214 PTA-10215
% 18:2 0.00 0.00 0.00 0.00
% 18:3 n-6 0.00 0.00 0.00 0.00
% 18:3 n-3 0.00 0.00 0.00 0.00
% 18:4 n-3 0.00 0.00 0.00 0.00
% 20:0 0.00 0.00 0.00 0.00
% 20: 1 n-9 0.00 0.00 0.00 0.00
% 20:2 0.00 0.00 0.00 0.00
% 20:3 n-9 0.00 0.00 0.00 0.00
% 20:3 n-6 0.00 0.00 0.00 0.00
% 20:3 n-3 0.90 0.77 0.99 0.66
% 20:4
ARA 1 .43 1 .32 1.65 0.72
% 20:5 n-3
EPA 13.33 14.93 14.14 8.54
% 22:0 0.00 0.00 0.00 0.00
% 22:1 0.00 0.00 0.00 0.00
% 22:2 0.00 0.00 0.00 0.00
% 22:3 0.00 0.00 0.00 0.00
% 22:4 n-6 0.00 0.00 0.00 0.00
% 22:5 n-6 2.39 1 .95 2.59 2.18
% 22:5 n-3 0.73 0.79 0.80 0.68
% 22:6 n-3
DHA 59.18 54.31 59.89 56.39
% 24:0 0.00 0.00 0.00 0.00
% 24:1 0.00 0.00 0.00 0.00
% Fat 45.69 38.08 42.88 48.48
% Unknown 1 .38 1 .58 1.27 2.19
[0183] All of the various aspects, embodiments, and options described herein can be combined in any and all variations.
[0184] All publications, patents, and patent applications mentioned in this specification are herein incorporated by reference to the same extent as if each individual publication, patent, or patent application was specifically and individually indicated to be incorporated by reference.

Claims

WHAT IS CLAIMED:
An isolated microorganism of the species deposited under ATCC Accession No. PTA- 10212.
An isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA-10212.
An isolated microorganism comprising an 18s rRNA comprising a polynucleotide sequence of SEQ ID NO: l or a polynucleotide sequence having at least 94% identity to SEQ ID NO: l .
An isolated microorganism comprising an 18s rRNA polynucleotide sequence that has at least 94% identity to an 18s rRNA polynucleotide sequence of the microorganism deposited under ATCC Accession No. PTA- 10212.
An isolated microorganism of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10% by weight eicosapentaenoic acid.
An isolated microorganism having the characteristics of the species deposited under ATCC Accession No. PTA- 10208, wherein the total fatty acids produced by the microorganism comprises more than about 10% by weight eicosapentaenoic acid.
An isolated microorganism that produces a triacylglycerol fraction, wherein eicosapentaenoic acid content of the triacylglycerol fraction is at least about 12% by weight.
The isolated microorganism of any one of claims 1 to 7, wherein the microorganism is a mutant strain.
9. An isolated microorganism deposited under ATCC Accession No. PTA-10212.
10. An isolated microorganism deposited under ATCC Accession No. PTA-10213.
1 1. An isolated microorganism deposited under ATCC Accession No. PTA-10214.
12. An isolated microorganism deposited under ATCC Accession No. PTA-10215.
13. An isolated microorganism deposited under ATCC Accession No. PTA- 10208.
14. An isolated microorganism deposited under ATCC Accession No. PTA- 10209.
15. An isolated microorganism deposited under ATCC Accession No. PTA- 10210.
16. An isolated microorganism deposited under ATCC Accession No. PTA- 1021 1.
17. A biomass comprising the microorganism of any one of claims 1 to 16 or mixtures thereof.
18. An isolated biomass, wherein at least about 20% by weight of a dry cell weight of the biomass are fatty acids, wherein more than about 10% by weight of fatty acids is eicosapentaenoic acid, and wherein the fatty acids comprise less than about 5% by weight each of arachidonic acid and docosapentaenoic acid n-6.
19. The isolated biomass of claim 18, wherein at least about 25%0 by weight of the fatty acids is docosahexaenoic acid.
20. An isolated biomass comprising triacylglycerol, wherein at least about 12% by weight of triacylglycerol is eicosapentaenoic acid.
21. The isolated biomass of any one of claims 18 to 20, wherein the fatty acids comprise less than about 5% by weight each of oleic acid, linoleic acid, linolenic acid, eicosenoic acid, and erucic acid.
22. An isolated culture comprising the microorganism of any one of claims 1 to 16 or mixtures thereof.
23. A food product, cosmetic, or pharmaceutical composition for a non-human animal or human, comprising the microorganism or biomass of any one of claims 1 to 21 or mixtures thereof.
24. A microbial oil comprising at least about 20% by weight eicosapentaenoic acid and less than about 5% by weight each of arachidonic acid, docosapentaenoic acid n-6, oleic acid, linoleic acid, linolenic acid, eicosenoic acid, erucic acid, and stearidonic acid.
25. The microbial oil of claim 24, further comprising at least about 25% by weight docosahexaenoic acid.
26. A microbial oil comprising a triacylglycerol fraction of at least about 10% by weight, wherein at least about 12% by weight of the fatty acids in the triacylglycerol fraction is eicosapentaenoic acid, wherein at least about 25% by weight of the fatty acids in the triacylglycerol fraction is docosahexaenoic acid, and wherein less than about 5%> by weight of the fatty acids in the triacylglycerol fraction is arachidonic acid.
27. A food product, cosmetic, or pharmaceutical composition for a non-human animal or human, comprising the microbial oil of any one of claims 24 to 26.
28. The food product of claim 23 or claim 27, wherein the food product is an infant formula.
29. The food product of claim 28, wherein the infant formula is suitable for premature infants.
30. The food product of claim 23 or claim 27, wherein the food product is milk, a beverage, a therapeutic drink, a nutritional drink, or a combination thereof.
31. The food product of claim 23 or claim 27, wherein the food product is an additive for the non-human animal or human foods.
32. The food product of claim 23 or claim 27, wherein the food product is a nutritional supplement.
33. The food product of claim 23 or claim 27, wherein the food product is an animal feed.
34. The animal feed of claim 33, wherein the animal feed is an aquaculture feed.
35. The animal feed of claim 33, wherein the animal feed is a domestic animal feed, a zoological animal feed, a work animal feed, a livestock feed, or a combination thereof.
36. A method for producing a microbial oil comprising omega-3 fatty acids, the method comprising: growing the isolated microorganism of any one of claims 1 to 16 or mixtures thereof in a culture to produce an oil comprising omega-3 fatty acids.
37. The method of claim 36, further comprising extracting the oil.
38. A method for producing a microbial oil comprising omega-3 fatty acids, the method comprising extracting an oil comprising omega-3 fatty acids from the biomass of any one of claims 17 to 21.
39. A microbial oil produced by the method of any one of claims 36 to 38.
40. A method for producing the biomass of any one of claims 17 to 21 , comprising; growing the isolated microorganism of any one of claims 1 to 16 or mixtures thereof in a culture to produce a biomass.
41. A biomass produced by the method of claim 40.
42. A method of producing the mutant strain of claim 8, comprising: mutagenizing the microorganism of any of claims 1 to 16; and
isolating the mutant strain.
43. Use of the isolated microorganism, biomass, or microbial oil of any one of claims 1 to 21, 24-26, 39, and 41, or mixtures thereof, for the manufacture of a medicament for treatment of inflammation or a condition related thereto.
44. Use of the isolated microorganism, biomass, or microbial oil of any one of claims 1 to 21, 24-26, 39, and 41, or mixtures thereof, for treatment of inflammation or a condition related thereto.
45. The isolated microorganism, biomass, or microbial oil of any one of claims 1 to 21, 24- 26, 39, and 41, or mixtures thereof, for use in treatment of inflammation or a condition related thereto.
46. A method for treating inflammation or a condition related thereto in a subject in need thereof, comprising administering to the subject the isolated microorganism, biomass, or microbial oil of any one of claims 1 to 21, 24-26, 39, and 41 , or mixtures thereof, and a pharmaceutically acceptable carrier.
PCT/US2010/028175 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof WO2011090493A1 (en)

Priority Applications (17)

Application Number Priority Date Filing Date Title
KR1020127021791A KR20120133381A (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
BR122015020119A BR122015020119B8 (en) 2010-01-19 2010-03-22 microbial oil, food products for a non-human animal and isolated biomass
CN201080062727.2A CN102884201B (en) 2010-01-19 2010-03-22 Produce microorganism, lipid acid constituent and preparation method thereof and the purposes of timnodonic acid
EA201290656A EA031136B1 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
EP21196529.8A EP4056708A1 (en) 2010-01-19 2010-03-22 Isolated biomass from schizochytrium or thraustochytrium comprising epa and dha and its use in animal feed
CA2787344A CA2787344C (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
DK10844116.3T DK2526197T3 (en) 2010-01-19 2010-03-22 MICRO; PRODUCING EICOSAPENTAIC ACID AND DOCOSAHEXAENIC ACID, FATIC ACID COMPOSITIONS, AND METHODS FOR PREPARING AND USING THEREOF
EP10844116.3A EP2526197B1 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid- and docosahexaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
KR1020187025169A KR102447978B1 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
KR1020147033815A KR20150013667A (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
JP2012549979A JP5920890B2 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid producing microorganisms, fatty acid compositions, and methods for making them and their use
NZ601757A NZ601757A (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
AU2010343305A AU2010343305B2 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
MX2012008388A MX343403B (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof.
BR112012017831A BR112012017831B8 (en) 2010-01-19 2010-03-22 microbial oil, animal food and biomass comprising said microbial oil
KR1020177024272A KR102155409B1 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
PH12016501930A PH12016501930B1 (en) 2010-01-19 2016-09-29 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods or making and uses thereof

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US29645610P 2010-01-19 2010-01-19
US61/296,456 2010-01-19

Publications (1)

Publication Number Publication Date
WO2011090493A1 true WO2011090493A1 (en) 2011-07-28

Family

ID=44277725

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2010/028175 WO2011090493A1 (en) 2010-01-19 2010-03-22 Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof

Country Status (19)

Country Link
US (6) US9924733B2 (en)
EP (3) EP4056708A1 (en)
JP (4) JP5920890B2 (en)
KR (4) KR20120133381A (en)
CN (2) CN105360351A (en)
AR (1) AR077916A1 (en)
AU (1) AU2010343305B2 (en)
BR (2) BR112012017831B8 (en)
CA (3) CA2787344C (en)
CL (2) CL2012002013A1 (en)
DK (1) DK2526197T3 (en)
EA (1) EA031136B1 (en)
HK (1) HK1221873A1 (en)
MX (1) MX343403B (en)
MY (1) MY160121A (en)
NZ (2) NZ626633A (en)
PH (1) PH12016501930B1 (en)
TW (2) TWI649424B (en)
WO (1) WO2011090493A1 (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2734630A4 (en) * 2011-07-21 2015-07-29 Dsm Ip Assets Bv Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
EP2952183A1 (en) * 2011-07-21 2015-12-09 DSM IP Assets B.V. Fatty acid compositions
JP2017213008A (en) * 2009-03-19 2017-12-07 ディーエスエム アイピー アセッツ ビー．ブイ． Polyunsaturated fatty acid synthase nucleic acid molecules and polypeptides, compositions, and methods of making and uses thereof
US10342772B2 (en) 2013-12-20 2019-07-09 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US10364207B2 (en) 2013-12-20 2019-07-30 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US10392578B2 (en) 2010-06-01 2019-08-27 Dsm Ip Assets B.V. Extraction of lipid from cells and products therefrom
US10472316B2 (en) 2013-12-20 2019-11-12 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US10798952B2 (en) 2010-01-19 2020-10-13 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
US11124736B2 (en) 2013-12-20 2021-09-21 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US12104139B2 (en) 2013-12-20 2024-10-01 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8207363B2 (en) 2009-03-19 2012-06-26 Martek Biosciences Corporation Thraustochytrids, fatty acid compositions, and methods of making and uses thereof
JP2014520574A (en) * 2011-07-21 2014-08-25 ディーエスエム アイピー アセッツ ビー．ブイ． Microbial oil enriched with polyunsaturated fatty acids
EP2826384A1 (en) 2013-07-16 2015-01-21 Evonik Industries AG Method for drying biomass
BR112016014262B1 (en) * 2013-12-20 2022-04-05 MARA Renewables Corporation METHOD TO RECOVER LIPIDS FROM A POPULATION OF MICRO-ORGANISMS
CN106793803B (en) 2014-10-02 2021-03-09 赢创运营有限公司 Method for producing PUFA-containing feed by extruding PUFA-containing biomass
CA2958439C (en) 2014-10-02 2022-09-20 Evonik Industries Ag Feedstuff of high abrasion resistance and good stability in water, containing pufas
ES2900848T3 (en) 2014-10-02 2022-03-18 Evonik Operations Gmbh Procedure for the production of a feed
WO2016050552A1 (en) 2014-10-02 2016-04-07 Evonik Degussa Gmbh Process for producing a pufa-containing biomass which has high cell stability
AU2015359335B2 (en) * 2014-12-12 2019-11-14 Dsm Ip Assets B.V. Feed supplement material for use in aquaculture feed
JPWO2017006918A1 (en) * 2015-07-03 2018-05-24 国立大学法人九州大学 Microbial oil-producing labyrinthulas, microbial oils, methods for their preparation and their use
WO2017055169A1 (en) * 2015-10-01 2017-04-06 Dsm Ip Assets B.V. Supplement material for use in pet food
ES2930078T3 (en) 2016-05-12 2022-12-07 Dsm Ip Assets Bv Method to increase the production of omega-3 polyunsaturated fatty acids in microalgae
RU2764558C2 (en) * 2016-12-15 2022-01-18 Сосьете Де Продюи Нестле С.А. Compositions and methods regulating digestibility in companion animal
DK3665296T3 (en) * 2017-08-10 2022-07-11 Dsm Ip Assets Bv DOUBLE CENTRIFUGATION PROCEDURE FOR PURIFICATION OF NOURISHING OIL
US20210401731A1 (en) * 2020-06-24 2021-12-30 Marco Ruggiero Anti-Aging Formula
SE2151489A1 (en) * 2021-12-07 2023-06-08 Mycorena Ab A food product or food ingredient comprising fungi biomass with an increased intracellular fat content
KR20240141784A (en) 2022-01-25 2024-09-27 디에스엠 아이피 어셋츠 비.브이. Media adjustment and nutrient supply approaches to increase polyunsaturated fatty acid production

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007068997A2 (en) * 2005-12-16 2007-06-21 Avestha Gengraine Technologies Pvt.Ltd. Docosahexaenoic acid (dha) producing thraustochytrid strain - sc1
US20080076164A1 (en) * 2004-07-16 2008-03-27 Petra Cirpus Method for Increasing the Content of Polyunsaturated Long-Chained Fatty Acids in Transgenic Organisms
US20080199923A1 (en) * 1992-10-16 2008-08-21 Martek Biosciences Corporation Process for the Heterotrophic Production of Microbial Products with High Concentrations of Omega-3 Highly Unsaturated Fatty Acids
US20090004219A1 (en) * 2005-12-29 2009-01-01 Abl Biotechnologies Ltd. Novel Strain of Schizochytrium limacinum useful in the production of lipids and Extracellular Polysaccharides and process thereof
US20090192304A1 (en) * 2001-04-16 2009-07-30 Martek Biosciences Corporation Product and Process for Transformation of Thraustochytriales Microorganisms

Family Cites Families (107)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4485173A (en) 1981-01-19 1984-11-27 Cpc International Inc. Preparation of fats and oils
CA1317901C (en) 1986-07-08 1993-05-18 Yoshifumi Shinmen Process for production of bishomo-_-linolenic acid and eicosapentaenoic acid
ES2061519T3 (en) 1986-12-26 1994-12-16 Sagami Chem Res PROCEDURE FOR THE PRODUCTION OF EICOSAPENTAENOIC ACID.
US5246841A (en) 1986-12-26 1993-09-21 Sagami Chemical Research Center Microbial process for production of eicosapentaenoic acid
JP2746371B2 (en) 1987-12-21 1998-05-06 サントリー株式会社 Bishomo-γ-linolenic acid and method for producing lipid containing the same
JP2710344B2 (en) 1988-07-13 1998-02-10 サントリー株式会社 Method for producing polyunsaturated fatty acid and lipid containing the same
US6451567B1 (en) 1988-09-07 2002-09-17 Omegatech, Inc. Fermentation process for producing long chain omega-3 fatty acids with euryhaline microorganisms
US5340594A (en) 1988-09-07 1994-08-23 Omegatech Inc. Food product having high concentrations of omega-3 highly unsaturated fatty acids
US5698244A (en) 1988-09-07 1997-12-16 Omegatech Inc. Method for raising animals having high concentrations of omega-3 highly unsaturated fatty acids
US5130242A (en) * 1988-09-07 1992-07-14 Phycotech, Inc. Process for the heterotrophic production of microbial products with high concentrations of omega-3 highly unsaturated fatty acids
US5244921A (en) 1990-03-21 1993-09-14 Martek Corporation Eicosapentaenoic acids and methods for their production
AU661297B2 (en) * 1991-01-24 1995-07-20 Martek Corporation Microbial oil mixtures and uses thereof
JPH078215A (en) 1993-04-30 1995-01-13 Kawasaki Steel Corp Marine microalgal food raw material containing docosahexaenoic acid and its production
WO1996033263A1 (en) 1995-04-17 1996-10-24 JAPAN, represented by DIRECTOR-GENERAL OF AGENCY OF INDUSTRIAL SCIENCE AND TECHNOLOGY Novel microorganisms capable of producing highly unsaturated fatty acids and process for producing highly unsaturated fatty acids by using the microorganisms
GB9514649D0 (en) 1995-07-18 1995-09-13 Zeneca Ltd Extraction of triglycerides from microorganisms
US6255505B1 (en) 1996-03-28 2001-07-03 Gist-Brocades, B.V. Microbial polyunsaturated fatty acid containing oil from pasteurised biomass
EP2251410A3 (en) 1996-03-28 2011-09-28 DSM IP Assets B.V. Preparation of microbial polyunsaturated fatty acid containing oil from pasteurised biomass
US20030143659A1 (en) 1996-03-28 2003-07-31 Hendrik Louis Bijl Process for the preparation of a granular microbial biomass and isolation of a compound thereform
EP0935667B1 (en) * 1996-07-23 2006-12-06 Nagase Chemtex Corporation Process for preparing docosahexaenoic acid and docosapentaenoic acid
PT960943E (en) 1996-12-27 2014-04-29 Suntory Holdings Ltd Media for culturing microorganisms and process for producing unsaturated fatty acids or lipids containing the same
JP2001512029A (en) 1997-08-01 2001-08-21 マーテック・バイオサイエンスィズ・コーポレーション DHA-containing nutritional compositions and methods for their production
EP1025842B1 (en) 1997-10-30 2004-07-21 Morishita Jintan Co., Ltd. Double-leyered capsule of unsaturated fatty acid or derivative thereof and process for producing the same
JP4079494B2 (en) * 1998-03-04 2008-04-23 サントリー株式会社 Method for producing arachidonic acid and / or eicosapentaenoic acid-containing fats and oils
JP4175698B2 (en) 1998-06-19 2008-11-05 サントリー株式会社 Novel triglyceride and composition containing the same
US8003772B2 (en) * 1999-01-14 2011-08-23 Martek Biosciences Corporation Chimeric PUFA polyketide synthase systems and uses thereof
KR100504324B1 (en) 1999-03-04 2005-07-28 산토리 가부시키가이샤 Utilization of material containing docosapentaenoic acid
IL143421A0 (en) 1999-09-29 2002-04-21 Micro Gaia Co Ltd Method for culturing algae
WO2001051598A1 (en) 2000-01-11 2001-07-19 Monsanto Technology Llc Process for making an enriched mixture of polyunsaturated fatty acid esters
MX350779B (en) 2000-01-19 2017-09-18 Dsm Ip Assets B V * Solventless extraction process.
EP1251744B2 (en) 2000-01-28 2015-08-26 DSM IP Assets B.V. Enhanced production of lipids containing polyenoic fatty acids by high density cultures of eukaryotic microbes in fermentors
JP2003523765A (en) 2000-02-24 2003-08-12 ロング，トーマス・ビーチ，ザセカンド Production method of carotenoid, xanthophyll and apo-carotenoid using eukaryotic microorganism
DE60020271T2 (en) 2000-03-29 2006-03-23 Council Of Scientific And Industrial Research PROCESS FOR INCREASING MULTIPLE-SATURATED FATTY ACIDS IN THRUSTOCHYTRIDES
US6410282B1 (en) * 2000-03-30 2002-06-25 Council Of Scientific And Industrial Research Method for enhancing levels of polyunsaturated fatty acids in thraustochytrid fungi
JP3425622B2 (en) 2000-03-30 2003-07-14 独立行政法人産業技術総合研究所 Cultures containing polyunsaturated fatty acids and methods for producing oils and fats containing polyunsaturated fatty acids using Labyrinthula
EP1178118A1 (en) 2000-08-02 2002-02-06 Dsm N.V. Isolation of microbial oils
DK1239022T3 (en) * 2001-03-09 2009-07-20 Nestle Sa Oil containing one or more long-chain polyunsaturated fatty acids derived from biomass, process for manufacture, food, food composition, cosmetic composition or pharmaceutical composition containing it
JP4995377B2 (en) 2001-04-26 2012-08-08 花王株式会社 Oil composition
AU2002309856B2 (en) 2001-05-14 2008-10-23 Dsm Ip Assets B.V. Production and use of a polar lipid-rich fraction containing omega-3 and/or omega-6 highly unsaturated fatty acids from microbes, genetically modified plant seeds and marine organisms
US7538238B2 (en) 2001-07-02 2009-05-26 Suntory Limited Production method of oil or fat containing polyunsaturated fatty acid-containing triglyceride
WO2003017945A2 (en) * 2001-08-24 2003-03-06 Martek Biosciences Boulder Corporation Products containing highly unsaturated fatty acids for use by women and their children during stages of preconception, pregnancy and lactation/post-partum
DE10151155A1 (en) 2001-10-19 2003-05-08 Nutrinova Gmbh Native PUFA triglyceride mixtures with a high content of polyunsaturated fatty acids as well as processes for their production and their use
US6677470B2 (en) 2001-11-20 2004-01-13 Natural Asa Functional acylglycerides
CA2469647C (en) * 2001-12-12 2011-02-15 Daniel G. Dueppen Extraction and winterization of lipids from oilseed and microbial sources
US20040203120A1 (en) 2002-03-22 2004-10-14 Council Of Scientific And Industrial Research Method for enhancing levels of polyunsaturated fatty acids in thraustochytrid protists
ES2391381T3 (en) 2002-05-03 2012-11-23 Martek Biosciences Corporation High quality lipids and methods for their production by enzymatic release from biomass
KR20140023448A (en) 2002-06-19 2014-02-26 디에스엠 아이피 어셋츠 비.브이. Preparation of microbial oil containing polyunsaturated fatty acids
DK1396533T3 (en) * 2002-09-04 2009-01-12 Nestec Sa Process for preparing an oil containing one or more polyunsaturated long chain fatty acids from biomass, foodstuffs and nutritious, cosmetic or pharmaceutical compositions containing this
CA2498569C (en) 2002-09-13 2016-11-29 Suntory Limited Process for production of transesterified oils/fats or triglycerides
CN112176006A (en) 2002-10-11 2021-01-05 日本水产株式会社 Process for the preparation of microbial oils with reduced unsaponifiable matter content and said oils
RU2235481C2 (en) 2002-11-20 2004-09-10 Общество с ограниченной ответственностью "Гелла-Фарма" Method for obtaining food biologically active additive (variants)
JP4280158B2 (en) 2002-12-27 2009-06-17 富士フイルム株式会社 Microorganisms capable of producing docosahexaenoic acid and use thereof
MY144341A (en) 2003-03-27 2011-08-29 Suntory Holdings Ltd Lipid-improving agent and composition containing lipid-improving agent
US20050019880A1 (en) 2003-03-31 2005-01-27 Council Of Scientific And Industrial Research Method of enhancing levels of polyunsaturated fatty acids in thraustochytrid protists
US6846942B2 (en) 2003-05-20 2005-01-25 David Rubin Method for preparing pure EPA and pure DHA
WO2005021735A1 (en) 2003-09-01 2005-03-10 Novozymes A/S Method for increasing yield of biomass of and/or components of biomass from marine microorganisms
KR101180594B1 (en) 2003-10-02 2012-09-06 마텍 바이오싸이언스스 코포레이션 Production of high levels of DHA in microalgae using modified amounts of chloride and potassium
DE10352838A1 (en) 2003-11-10 2005-07-07 Nutrinova Nutrition Specialties & Food Ingredients Gmbh A method of cultivating microorganisms of the genus Thraustochytriales using an optimized low salt medium
TWI365716B (en) 2003-12-02 2012-06-11 Suntory Holdings Ltd Oil or fat and oil compositions containing phospholipids and a long-chain polyunsaturated fatty acid supply compound, and food using same
SE0303513D0 (en) 2003-12-19 2003-12-19 Pronova Biocare As Use of a fatty acid composition comprising at least one of epa and any or any combination thereof
EP1706500B1 (en) 2003-12-30 2010-09-08 DSM IP Assets B.V. Deaeration process
GB0403247D0 (en) 2004-02-13 2004-03-17 Tillotts Pharma Ag A pharmaceutical composition
DK1776450T3 (en) 2004-08-12 2010-06-21 Nippon Suisan Kaisha Ltd Process for polyunsaturated fatty acid production using novel cell preservation technique
US20080269329A1 (en) * 2004-08-24 2008-10-30 Shigeaki Fujikawa Process for Production of Microbial Fat/Oil Containing Discretional Amount of Diacylglycerol and Said Fat/Oil
JP4624040B2 (en) 2004-09-06 2011-02-02 日本水産株式会社 Cell culture method
CA2586309C (en) 2004-11-04 2014-05-27 Monsanto Technology Llc High pufa oil compositions
US7588931B2 (en) 2004-11-04 2009-09-15 E. I. Du Pont De Nemours And Company High arachidonic acid producing strains of Yarrowia lipolytica
US8241868B2 (en) 2005-02-08 2012-08-14 Nippon Suisan Kaisha, Ltd. Production of polyunsaturated fatty acids using cell treatment method
PL2447356T3 (en) 2005-06-07 2016-10-31 Eukaryotic microorganisms for producing lipids and antioxidants
CN101252844A (en) * 2005-07-01 2008-08-27 马泰克生物科学公司 Polyunsaturated fatty acid-containing oil product and uses and production thereof
EA200800225A1 (en) 2005-07-01 2008-06-30 Мартек Байосайенсиз Корпорейшн CONTAINING POLYUNSATURATED FATTY ACIDS, OIL PRODUCT AND ITS APPLICATIONS AND OBTAINING
CN101272999B (en) 2005-07-12 2013-01-23 阿德莱德研究和创新私人有限公司 Chelating agents for micronutrient fertilizers
EP1968402A2 (en) 2005-10-07 2008-09-17 Ocean Nutrition Canada Limited Salts of fatty acids and methods of making and using thereof
US9265745B2 (en) 2005-12-21 2016-02-23 Brudy Technology S.L. Use of DHA, EPA or DHA-derived EPA for treating a pathology associated with cellular oxidative damage
CN101466270A (en) 2006-04-11 2009-06-24 马泰克生物科学公司 Food products comprising long chain polyunsaturated fatty acids and methods for preparing the same
EP2046136A2 (en) 2006-06-23 2009-04-15 The Procter and Gamble Company Concentrated and odorless omega 3 fatty acids
AU2007270135B9 (en) 2006-07-05 2013-06-27 Fermentalg Production of ultrapure EPA and polar lipids from largely heterotrophic culture
WO2008012329A2 (en) 2006-07-28 2008-01-31 V. Mane Fils Seamless capsules containing high amounts of polyunsaturated fatty acids and a flavouring component
CN101981201A (en) * 2006-08-01 2011-02-23 加拿大海洋营养食品有限公司 Oil producing microbes and methods of modification thereof
JP2010502189A (en) * 2006-08-29 2010-01-28 マーテック バイオサイエンシーズ コーポレーション Use of DPA (n-6) oil in infant formula
CN101617040B (en) 2006-10-30 2012-07-04 纳幕尔杜邦公司 Delta17 desaturase and its use in making polyunsaturated fatty acids
US8936923B2 (en) 2006-12-05 2015-01-20 Biomass Research & Refining Pty Ltd Production of biodiesel
JP5101894B2 (en) 2007-01-15 2012-12-19 サントリーホールディングス株式会社 Polyunsaturated fatty acid and method for producing lipid containing the same
US20080234377A1 (en) 2007-03-23 2008-09-25 Martek Biosciences Corporation Polyunsaturated fatty acids for treatment of dementia and pre-dementia-related conditions
EP1992233A1 (en) 2007-05-11 2008-11-19 DSMIP Assets B.V. Stabilized marine oils and process of making them
WO2009002145A1 (en) 2007-06-26 2008-12-31 N.V. Nutricia Lipid composition for improving function of brain functioning
US20090011012A1 (en) 2007-07-06 2009-01-08 Baum Seth J Fatty acid compositions and methods of use
NZ584460A (en) 2007-09-12 2012-10-26 Martek Biosciences Corp Biological oil produced by a microorganism of the kingdom Stramenopil by heterotropic fermentation
US20090099261A1 (en) 2007-09-25 2009-04-16 Isi Brands Inc. Omega-3 mixtures
JP5711968B2 (en) * 2007-10-03 2015-05-07 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニーＥ．Ｉ．Ｄｕ Ｐｏｎｔ Ｄｅ Ｎｅｍｏｕｒｓ Ａｎｄ Ｃｏｍｐａｎｙ An optimized strain of Yarrowia Lipolytica to produce high eicosapentaenoic acid
US8343753B2 (en) 2007-11-01 2013-01-01 Wake Forest University School Of Medicine Compositions, methods, and kits for polyunsaturated fatty acids from microalgae
DE102008042932A1 (en) 2008-10-17 2010-04-22 Evonik Degussa Gmbh Production and use of methionylmethionine as a feed additive for fish and crustaceans
ES2583639T3 (en) * 2008-11-28 2016-09-21 Terravia Holdings, Inc. Production of specific oils in heterotrophic microorganisms
US20100178369A1 (en) 2009-01-15 2010-07-15 Nicole Lee Arledge Antioxidant-stabilized concentrated fish oil
CN102333880A (en) 2009-02-25 2012-01-25 V.B.医疗私人有限公司 Improved methods for fermentative production of docosahexaenoic acid
WO2010103402A1 (en) 2009-03-09 2010-09-16 Pronova Biopharma Norge As Compositions comprising a fatty acid oil mixture comprising epa and dha in free acid form and a surfactant, and methods and uses thereof
US8207363B2 (en) 2009-03-19 2012-06-26 Martek Biosciences Corporation Thraustochytrids, fatty acid compositions, and methods of making and uses thereof
EP3192871B1 (en) 2009-03-19 2019-01-23 DSM IP Assets B.V. Polyunsaturated fatty acid synthase nucleic acid molecules and polypeptides, compositions, and methods of making and uses thereof
CA2754952C (en) 2009-03-19 2018-11-06 Martek Biosciences Corporation Thraustochytrids, fatty acid compositions, and methods of making and uses thereof
WO2011047259A1 (en) 2009-10-16 2011-04-21 Glaxosmithkline Llc Compositions
US20110195449A1 (en) 2009-12-28 2011-08-11 Martek Biosciences Corporation Recombinant Thraustochytrids that Grow on Sucrose, and Compositions, Methods of Making, and Uses Thereof
US9012197B2 (en) 2009-12-28 2015-04-21 Merial, Inc. Production of hemagglutinin-neuraminidase protein in microalgae
CA2787344C (en) 2010-01-19 2018-03-20 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
EP2576801B1 (en) 2010-06-01 2019-10-02 DSM IP Assets B.V. Extraction of lipid from cells and products therefrom
US9222112B2 (en) 2011-07-21 2015-12-29 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
JP2014520574A (en) * 2011-07-21 2014-08-25 ディーエスエム アイピー アセッツ ビー．ブイ． Microbial oil enriched with polyunsaturated fatty acids
DK3050972T3 (en) * 2011-07-21 2021-02-08 Dsm Ip Assets Bv PROCEDURES FOR THE PREPARATION OF EICOSAPENTAIC ACID IN THRAUSTOCHYTRIDES
CN107429196B (en) * 2015-02-09 2021-07-16 阿彻丹尼尔斯米德兰德公司 Renewable-derived polymer oil macroinitiators and thermoplastic block copolymers derived therefrom

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080199923A1 (en) * 1992-10-16 2008-08-21 Martek Biosciences Corporation Process for the Heterotrophic Production of Microbial Products with High Concentrations of Omega-3 Highly Unsaturated Fatty Acids
US20090192304A1 (en) * 2001-04-16 2009-07-30 Martek Biosciences Corporation Product and Process for Transformation of Thraustochytriales Microorganisms
US20080076164A1 (en) * 2004-07-16 2008-03-27 Petra Cirpus Method for Increasing the Content of Polyunsaturated Long-Chained Fatty Acids in Transgenic Organisms
WO2007068997A2 (en) * 2005-12-16 2007-06-21 Avestha Gengraine Technologies Pvt.Ltd. Docosahexaenoic acid (dha) producing thraustochytrid strain - sc1
US20090004219A1 (en) * 2005-12-29 2009-01-01 Abl Biotechnologies Ltd. Novel Strain of Schizochytrium limacinum useful in the production of lipids and Extracellular Polysaccharides and process thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
DATABASE GENBANK 31 July 2001 (2001-07-31), RAGAN ET AL.: "Labyrinthulid quahog parasite QPX small subunit ribosomal RNA gene, complete sequence.", XP008169054, Database accession no. AF261664 *
See also references of EP2526197A4 *

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2017213008A (en) * 2009-03-19 2017-12-07 ディーエスエム アイピー アセッツ ビー．ブイ． Polyunsaturated fatty acid synthase nucleic acid molecules and polypeptides, compositions, and methods of making and uses thereof
US10798952B2 (en) 2010-01-19 2020-10-13 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
US11154076B2 (en) 2010-01-19 2021-10-26 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
US10392578B2 (en) 2010-06-01 2019-08-27 Dsm Ip Assets B.V. Extraction of lipid from cells and products therefrom
EP3050972A3 (en) * 2011-07-21 2016-11-02 DSM IP Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
EP2952183A1 (en) * 2011-07-21 2015-12-09 DSM IP Assets B.V. Fatty acid compositions
US10272060B2 (en) 2011-07-21 2019-04-30 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
EP2734630A4 (en) * 2011-07-21 2015-07-29 Dsm Ip Assets Bv Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
US10925850B2 (en) 2011-07-21 2021-02-23 Dsm Ip Assets B.V. Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
US10342772B2 (en) 2013-12-20 2019-07-09 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US10364207B2 (en) 2013-12-20 2019-07-30 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US10472316B2 (en) 2013-12-20 2019-11-12 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US11124736B2 (en) 2013-12-20 2021-09-21 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells
US12104139B2 (en) 2013-12-20 2024-10-01 Dsm Ip Assets B.V. Processes for obtaining microbial oil from microbial cells

Also Published As

Publication number Publication date
JP2020072676A (en) 2020-05-14
JP2016052311A (en) 2016-04-14
KR20170104628A (en) 2017-09-15
AR077916A1 (en) 2011-10-05
KR20180100714A (en) 2018-09-11
CN102884201B (en) 2016-04-13
KR20120133381A (en) 2012-12-10
MY160121A (en) 2017-02-28
JP2013516997A (en) 2013-05-16
CL2012002013A1 (en) 2013-03-22
PH12016501930A1 (en) 2019-02-11
BR122015020119B1 (en) 2021-04-13
TW201125986A (en) 2011-08-01
US20110177031A1 (en) 2011-07-21
CL2015001281A1 (en) 2015-08-07
TWI653336B (en) 2019-03-11
EA031136B1 (en) 2018-11-30
US20170164639A1 (en) 2017-06-15
US11154076B2 (en) 2021-10-26
BR112012017831A2 (en) 2015-10-06
EP2526197A1 (en) 2012-11-28
CA2993690C (en) 2022-03-22
NZ601757A (en) 2015-01-30
KR102447978B1 (en) 2022-09-27
EP3054016A2 (en) 2016-08-10
KR102155409B1 (en) 2020-09-11
JP5920890B2 (en) 2016-05-18
BR112012017831B8 (en) 2021-05-25
US20150237888A1 (en) 2015-08-27
BR112012017831B1 (en) 2021-03-09
TWI649424B (en) 2019-02-01
JP6705599B2 (en) 2020-06-03
US9924733B2 (en) 2018-03-27
US20180295860A1 (en) 2018-10-18
US10798952B2 (en) 2020-10-13
BR112012017831A8 (en) 2018-06-26
EP4056708A1 (en) 2022-09-14
AU2010343305A1 (en) 2012-09-06
MX343403B (en) 2016-11-03
CA2787344C (en) 2018-03-20
BR122015020119A2 (en) 2015-12-29
US20220000147A1 (en) 2022-01-06
EP2526197B1 (en) 2018-06-20
CA2896012A1 (en) 2011-07-28
US9668499B2 (en) 2017-06-06
CN105360351A (en) 2016-03-02
US20150313861A1 (en) 2015-11-05
EA201290656A1 (en) 2013-02-28
AU2010343305B2 (en) 2015-06-11
KR20150013667A (en) 2015-02-05
TW201730343A (en) 2017-09-01
PH12016501930B1 (en) 2019-02-11
NZ626633A (en) 2015-10-30
BR122015020119B8 (en) 2021-05-04
CA2787344A1 (en) 2011-07-28
CA2993690A1 (en) 2011-07-28
MX2012008388A (en) 2012-08-15
CA2896012C (en) 2017-08-01
DK2526197T3 (en) 2018-10-01
HK1221873A1 (en) 2017-06-16
CN102884201A (en) 2013-01-16
EP2526197A4 (en) 2014-05-21
JP2018078900A (en) 2018-05-24
EP3054016A3 (en) 2016-11-30

Similar Documents

Publication Publication Date Title
US11154076B2 (en) Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
US10925850B2 (en) Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
AU2017202422B2 (en) Eicosapentaenoic acid-producing microorganisms, fatty acid compositions, and methods of making and uses thereof
NZ619872B2 (en) Microbial oil compositions containing omega-3 polyunsaturated fatty acids and dosage forms containing such oils.

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 201080062727.2

Country of ref document: CN

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10844116

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2787344

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 2012549979

Country of ref document: JP

Ref document number: 12012501469

Country of ref document: PH

Ref document number: MX/A/2012/008388

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 2012002013

Country of ref document: CL

Ref document number: 1201003612

Country of ref document: TH

WWE Wipo information: entry into national phase

Ref document number: 2010343305

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: 7056/DELNP/2012

Country of ref document: IN

WWE Wipo information: entry into national phase

Ref document number: 201290656

Country of ref document: EA

WWE Wipo information: entry into national phase

Ref document number: 2010844116

Country of ref document: EP

ENP Entry into the national phase

Ref document number: 20127021791

Country of ref document: KR

Kind code of ref document: A

ENP Entry into the national phase

Ref document number: 2010343305

Country of ref document: AU

Date of ref document: 20100322

Kind code of ref document: A

REG Reference to national code

Ref country code: BR

Ref legal event code: B01A

Ref document number: 112012017831

Country of ref document: BR

ENP Entry into the national phase

Ref document number: 112012017831

Country of ref document: BR

Kind code of ref document: A2

Effective date: 20120718

WWE Wipo information: entry into national phase

Ref document number: 12016501930

Country of ref document: PH