WO2004047554A1 - Marine lipid compositions - Google Patents
Marine lipid compositions Download PDFInfo
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- WO2004047554A1 WO2004047554A1 PCT/EP2003/013299 EP0313299W WO2004047554A1 WO 2004047554 A1 WO2004047554 A1 WO 2004047554A1 EP 0313299 W EP0313299 W EP 0313299W WO 2004047554 A1 WO2004047554 A1 WO 2004047554A1
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
- A23D9/00—Other edible oils or fats, e.g. shortenings or cooking oils
- A23D9/007—Other edible oils or fats, e.g. shortenings or cooking oils characterised by ingredients other than fatty acid triglycerides
- A23D9/013—Other fatty acid esters, e.g. phosphatides
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J7/00—Phosphatide compositions for foodstuffs, e.g. lecithin
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- 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
- A23K20/142—Amino acids; Derivatives thereof
- A23K20/147—Polymeric derivatives, e.g. peptides or proteins
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K40/00—Shaping or working-up of animal feeding-stuffs
- A23K40/10—Shaping or working-up of animal feeding-stuffs by agglomeration; by granulation, e.g. making powders
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K40/00—Shaping or working-up of animal feeding-stuffs
- A23K40/30—Shaping or working-up of animal feeding-stuffs by encapsulating; by coating
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- 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
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- 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
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- 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
- A23L33/12—Fatty acids or derivatives thereof
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- 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
- A23L33/17—Amino acids, peptides or proteins
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P1/00—Drugs for disorders of the alimentary tract or the digestive system
- A61P1/04—Drugs for disorders of the alimentary tract or the digestive system for ulcers, gastritis or reflux esophagitis, e.g. antacids, inhibitors of acid secretion, mucosal protectants
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P17/00—Drugs for dermatological disorders
- A61P17/04—Antipruritics
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P19/00—Drugs for skeletal disorders
- A61P19/02—Drugs for skeletal disorders for joint disorders, e.g. arthritis, arthrosis
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P25/00—Drugs for disorders of the nervous system
- A61P25/28—Drugs for disorders of the nervous system for treating neurodegenerative disorders of the central nervous system, e.g. nootropic agents, cognition enhancers, drugs for treating Alzheimer's disease or other forms of dementia
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- 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]
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- 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
- A61P3/06—Antihyperlipidemics
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P9/00—Drugs for disorders of the cardiovascular system
- A61P9/10—Drugs for disorders of the cardiovascular system for treating ischaemic or atherosclerotic diseases, e.g. antianginal drugs, coronary vasodilators, drugs for myocardial infarction, retinopathy, cerebrovascula insufficiency, renal arteriosclerosis
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P9/00—Drugs for disorders of the cardiovascular system
- A61P9/12—Antihypertensives
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- 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
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- 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
- C11B1/104—Production of fats or fatty oils from raw materials by extracting using super critical gases or vapours
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- 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
-
- 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
- This invention relates to marine phospholipid compositions (MPL) comprising long chain omega-3-fatty acids.
- MPL marine phospholipid compositions
- the compositions are particularly suitable as supplements for human consumption, animal feed or for nutritional and embedment purposes in feed compositions for aquatic livestock and fish larvae.
- Phospholipids are amphipathic lipids which are components of all cell membranes.
- the phospholipid molecule comprises a phosphoric acid ester head group attached to a glycerol backbone with one or more usually two fatty acid chains.
- the head group may be neutral, anionic, cationic or zwitterionic depending on the pH.
- the different types of phospholipids are identified by their head groups. Regardless of the source, the most widely occurring natural phospholipid is phosphatidylcholine (PC) which has chorine as a head group. The second most abundant is phospha ⁇ ylethanolamine (PE).
- PC phosphatidylcholine
- PE phospha ⁇ ylethanolamine
- Phosphatidyl inositol PI
- PS phosphatidyl serine
- SPM spl ingornyelin
- the chief difference between the phospholipids from different sources is reflected in the fatty acid profiles which vary according to chain length and degree of unsaturation.
- the fatty acid moieties attached to phospholipids from natural sources have 14 to 24 carbon atoms.
- the unsaturated fatty acids mostly comprise C18 to C22 chains and may contain between one to six double bonds depending on the origin, i.e. marine, artirnal, or plant.
- Plant derived phospholipids usually do not contain fatty acids with a chain length of more than 18 carbon atoms.
- about 65 wt% to 75 wt% of the fatty acids in soya (mainly C18) comprise one to three double bonds, approximately 60 wt% of which is the omega-6 linoleic acid with two double bonds.
- egg phospholipids additionally comprise some longer chain fatty acids (C20 and C22 with four and 6 double bonds respectively).
- Marine phospholipids are characterised by very high levels of mostly long chain C 20 and C22 highly unsaturated fatty acids (HUFA), eicosapentaenoic acid (EPA) and docosahexaenoic acid (DHA).
- HUFA highly unsaturated fatty acids
- EPA eicosapentaenoic acid
- DHA docosahexaenoic acid
- Soya and egg phospholipids are widely employed for their ubiquitous and multi-functional properties. They are used extensively in all types of applications in the food and feed industries particularly as emulsifiers because of their amphiphilic nature. They are also employed as a rich source of unsaturated fatty acids such as linoleic, linolenic (soya), arachidonic and docosahexaenoic acid (egg)in nutritional and functional foods. Phospholipids from plants do not contain the type of long chain highly unsaturated omega - 3- fatty acids found in fish oils. The level of HUFAs in marine phospholipids is higher than in the corresponding oily triglycerides from the same source.
- bioavailability of the fatty acids is believed to be higher from phospholipids compared to triglycerides. This may be due to the amphiphilic properties of phospholipids reflected in better water dispersibility and/ or their greater susceptibility to phospholipases compared to the glycerolysis of triglycerides.
- marine phospholipids would appear to offer an extremely rich source of long chain omega-3 polyunsaturated fatty acids for incorporation into fish diets and as supplements for humans.
- the prior art relating to marine phospholipids in aquaculture is chiefly concerned with preparing fish feed compositions from different marine sources and raw materials or biomass.
- WO 00/27218 describes a composite dry feed for fish larvae to replace live feed comprising a matrix containing water-insoluble nutrients and phospholipids embedded in the particles and a method of preparing the feed particles.
- WO 01/50884 describes a composite feed for feeding prey organisms suitable for aquaculture.
- the lipid component is derived from marine organisms such as fishmeal, phytoplankton or zoo plankton biomass.
- EP 0 996 740 provides a particulate material with high proportion of DHA in the lipid fraction and a mean particle size between 5 microns to 10 microns, suitable as a nutritional supplement in aquaculture.
- the method describes a protein/ phospholipid composition extracted from an aqueous suspension of broken algal cells using solvent extraction and removal of water by spray drying.
- Feed compositions for normal fish diets employ phospholipid mixtures (lecithin) from soya to emulsify Epophilic and hydrophilic components and hold them together in. the feed particles.
- phospholipid mixtures lecithin
- the high percentage of esterified polyunsaturated fatty acids, the bio-membrane forming properties on top of the emulsifying properties make marine phospholipids more effective to optimise nutritional properties and rninirnise leakage, particularly of water soluble nutrients.
- compositions comprising selected marine phospholipids and other components can form versatile lipid aggregates which will entrap both water soluble and oil soluble compounds either by association or solubilisation in addition to emulsification.
- the entrapment depends on the type of aggregates, which may be bilayered or icellar, vesicular or non vesicular, according to the composition of the phospholipid mixture.
- Liposo es are one example of vesicular structures whilst micro emulsion droplets, micelles and mixed micelles are examples of non vesicular structures useful for entrapment.
- lipid aggregates derived from the MPL compositions described in this invention is their unexpected capacity for containment of both hydrop ilic and Hpophilic aterials not only in human nutritional supplements and functional foods, but also in animal, fish and larvae feed compositions particularly in the presence of a destabilising medium like sea water.
- the invention is in the area of 'particulate' and 'waxy ' marine phospholipid compositions and ⁇ UFA concentrates' suitable as supplements in human nutrition and functional food and also for embedment and nutritional purposes in ariimal and fish feed microparticle compositions.
- the present invention relates to a marine phospholipid (MPL) composition suitable for human or aquaculture applications comprising a dry composition, i.e. in particulate or powdered form, comprising nutritional components selected from the group consisting of marine phospholipids, marine proteins ,amino acids, minerals prepared by solvent or gas extraction under super or hypercritical conditions of a dried marine raw materialcomprising a major amount of polar and a lower amount of non polar (neutral) lipids.
- the dried marine raw material has low moisture content i.e. below 10 wt%.
- composition comprises,
- 70 wt% to 95 wt% of the total lipids in I) consist of polar lipids and 5 wt% to 30 wt% consist of neutral lipids.
- the composition comprises,
- the invention also describes a particulate composition wherein 40 wt% to 80 wt% of the polar lipids consist of phosphatidylcholine or mixtures of PC and the monoacyl derivative thereof, wherein said phosphatidylcholine and the monoacyl derivative are esterified with 30 wt% to 60 wt% HUFA's.
- the balance of 20 wt% to 60 wt% of the polar lipids in the composition contain phospholipids selected from the group consisting of phosphatidyl ethanolamine (PE), phosphatidyl inositol (PI), phosphatidyl serine (PS), sphmgomyelin (SPM) and the monoacyl derivatives thereof.
- PE phosphatidyl ethanolamine
- PI phosphatidyl inositol
- PS phosphatidyl serine
- SPM sphmgomyelin
- the invention further describes a purified, viscous or paste-like, waxy MPL composition prepared by ethanol extraction from a particulate MPL composition.
- the waxy MPL composition contains, i) 70 wt% to 95 wt% or more of total lipids, ii) 5 wt% to 30 wt% of neutral lipids.
- the purified waxy MPL composition may be prepared by ethanol extraction of a dried composition comprising nutritional components selected from the group consisting of phospholipid/marine protein/ amino acid/ minerals blend.
- the composition preferably contains not more than 15 wt% neutral lipids and at least 40 wt% of phosphatidylcholine or mixture of PC and the monoacyl derivative thereof, calculated on the basis of all the phospholipids, wherein at least 30 wt% of the fatty acids are omega-3 fatty acids esterified to the phospholipids.
- the resulting waxy composition may be further blended with fish or vegetable oils to prepare a liquid composition that may be filled into hard or soft gelatine capsules or the like, as a supplement for human nutrition.
- the invention further provides water-dispersible marine phospholipid (MPL) concentrate in hydrophilic medium which may be prepared from a waxy composition for use in multicomponent fish and larvae feed compositions referred to as 'microparticles' for optimising the containment and retention of oil soluble and water soluble nutritional components.
- MPL water-dispersible marine phospholipid
- the embodiment includes a homogeneous water-dispersible concentrate which comprises: i) 25 wt% to 75 wt% of a marine phospholipid composition comprising PC or mixtures of PC and the monoacyl derivative in an amount of at least 40 wt% as the major component and minor amounts of a phospholipid selected from the group consisting of PE, PI, SPM and PS and their monoacyl derivatives, ii) 15 wt% to 75 wt% of ethanol or at least one polyol or mixtures thereof, iii) water to make 100%; and, optionally ,further additives selected from the group consisting of polymers, nutritional components, stabilisers, preservatives, and antioxidants.
- the invention also includes a method of preparing lipid aggregates for embedment in fish and larvae feed micro particles which comprises dispersing in water a lipid concentrate comprising, i) 25 wt% to 75 wt% of a marine phospholipid composition comprising PC or mixtures of PC and the monoacyl derivative in an amount of at least 40 wt% as the major component and minor amounts of at least one phospholipid selected from the group consisting of PE, PI,
- SPM and PS and their monoacyl derivatives ii) 15 wt% to 75 wt% of ethanol or at least one polyolor mixtures thereof, iii) water to make 100%, and, optionally, iv) further additives selected from the group consisting of polymers, nutritional components, stabilisers, preservatives, and antioxidants;
- MPLs are particularly useful as supplements to prevent coronary heart disease (CHD), to reduce elevated blood cholesterol and triglycerides, high blood pressure, high blood glucose and to treat several mental disorders (such as Alzheimer), premenstrual syndrome (PMS), inflammatory bowel disease, osteoarthritis, inflammatory skin diseases etc.
- CHD coronary heart disease
- PMS premenstrual syndrome
- Omega-3 fatty acids also need to be supplied in aquaculture diets because of the inability of fish larvae to synthesise these compounds de novo from shorter chain precursors. Lack of these essential fatty acids impair growth levels.
- the invention includes marine phospholipid blends which may be dry or waxy compositions and water dispersible concentrates in admixture with phospholipids selected from the group consisting of vegetable or egg phospholipids, enzyme modified phospholipids and synthetic and semi-synthetic phospholipids comprising C14 to C22 fatty acids with one to six double bonds, wherein the marine phospholipids preferably comprise the major component i.e. more than 50% by weight of the total mixture.
- the compositions may further comprise biologically active compounds.
- 'lecithin' is used as a broad definition to describe mixtures comprising phosphatidylcholine (PC) and other types of phospholipids. It is not used interchangeably as a narrow definition to describe only PC. It also covers mixtures of phospholipids from different sources and mixtures thereof;
- PC phosphatidylcholine
- 'marine phospholipid' refers to the phospholipid compositions comprising predominantly long chain and highly unsaturated fatty acids obtained from a 'marine raw material' e.g. roe and milt of fish such as salmon, herring, capelin, saithe and cod, etc. It includes phospholipids from all forms of marine vegetation and life forms such as krill and other crustaceans and those prepared by synthesis or partial synthesis (e.g. enzymatic fatty acid exchange) involving phospholipids from other sources and different species. The term also extends to blends of marine phospholipids and egg or soya phospholipids with the said MPL as the major component in the mixture.
- the phospholipid content may vary by up to +/- 25 wt% of the values normally quoted for different species depending on origin, source, climate and other seasonal factors.
- the definition also includes mixtures or blends comprising marine diacyl phospholipids and the monoacyl derivatives prepared by enzyme hydrolysis using phospholipase A2 on a suitable marine phospholipid substrate.
- 'polar lipids' are amphipatic lipids such as phospholipids, glycolipids and sphingolipids which are components of cell membranes from marine organisms;
- 'neutral lipids' are non polar lipids such as mono, di and triglycerides, free fatty acids and esters, cholesterol, cholesterol esters and carotenoids which are present in marine organisms;
- 'total lipids' are combined polar and neutral lipids
- marine proteins and amino acids refers to proteinaceous materials originating from marine organisms
- concentrate' describes a standardised and defined mixture prepared from purified MPL comprising HUFAs, predominantly DHA and EPA in a water dispersible hydrophilic medium.
- the concentrate may comprise a mixture of marine phospholipids blended with soya , egg, synthetic, semisynthetic,and enzyme modified phospholipids. It may be a liquid or gel like composition suitable for preparing multicomponent feed for aquatic lifestock including microparticles for fish larvae and weaning. It may also be administered as supplement for human use as such or in a unit dosage form.
- 'nutritional components' include all substances which are nutritionally valuable to humans, livestock, fish larvae, smelt and other marine species. Examples include phospholipids, proteins, amino acids, minerals, vitamins, fish protein hydrolysates, fish oil triglycerides and carbohydrates. Tong chain fatty acids' refer to fatty acids with more than 18 carbon atoms starting with eicosa (C20) and docosa (C22) fatty acids;
- 'highly unsaturated' fatty acids may have three or more usually four or more double bonds, e.g., tetraenoic(4), pentaenoic(5) and hexaenoic(6) which are either omega-6 or omega-3fatty acids.
- Eicosatetraenoic acid (AA) is an omega-6 fatty acid
- EPA eicosapentaenoic acid
- DHA docosahexaenoic acid
- 'fluid extraction' means 'de-oiling' or removal of neutral lipids from a dried marine raw material using a solvent in Hquid form, such as acetone , or a supercritical gas such as carbon dioxide, nitrous oxide or propane or mixtures thereof, under hypercritical (supercritical) conditions;
- a solvent in Hquid form such as acetone
- a supercritical gas such as carbon dioxide, nitrous oxide or propane or mixtures thereof, under hypercritical (supercritical) conditions
- 'ethanol extraction' describes the purification of a dry MPL composition after deoiling by using ethanol or related solvents such as methanol, isopropanol, tert-butanol, n-propanol and mixtures thereof to extract the polar lipids from proteins and amino acids and other impurities.
- a waxy MPL composition is obtained after removal of the ethanol or related solvent.
- composition' describes a dried, powdered composition with average particle diameter above 0.5 mm with moisture content that is below 10%.
- Standard procedures to obtain purified or semi-purified phospholipids particularly from soya and egg are based on a multi-step fractionation and/ or purification process starting from crude, commercial lecithins. Removal of lecithin from crude vegetable oils (Degumming)
- Vegetable lecithins may be obtained by simple water degurruning of crude oils or by other processes like specific centrifugation of the wet starting materials.
- it is not very satisfactory to utilise currently available procedures based on marine raw materials and biomass with high water content to prepare marine phospholipids for human nutrition and fish feed compositions without modification of the process.
- Improved extraction methods are therefore required for preparing MPL compositions with desirable amounts of polar lipids and low amounts of neutral lipids which are preferred in human nutriceutical and functional food applications and for forming lipid aggregates embedded in feed microparticles.
- Drying using elevated temperatures or spray drying is usually employed to prepare MPL containing powders from crude, aqueous fish roe and milt, or biomass from broken marine algal cells containing large amounts of water.
- alternative technologies for example freeze drying or other low stress drying methods to dry the marine raw materials so that they have lower amounts of water prior to processing.
- Preferred methods for the removal of neutral lipids, such as triglycerides, cholesterol and cholesterol esters, from the dry marine raw material are, fluid extraction with suitable liquids for instance acetone, and gases like carbon dioxide or other suitable gases under supercritical conditions.
- the product remaining after acetone or more preferably C0 2 extraction is a particulate composition comprising protein, amino acids, minerals, polar lipids and smaller (low) amounts of neutral lipids.
- the particulate MPL composition comprises 70 wt% to 90 wt% of marine protein and amino acids, preferably below 80 wt%.
- the polar and neutral lipids amount to 10 wt% to 30 wt%, preferably above 15 wt%.
- the polar lipids amount to 70 wt% to 95% wt%, preferably above 80 wt% of the total lipids whilst the neutral lipids make up the balance amounting to 5 wt% to 20 wt%, preferably below 15 wt%.
- the moisture content is below 10 wt% whilst minerals and trace elements based on ash residues make up less than 10 wt%.
- the composition may be used as such, in powder form in nutritional supplements, in unit dosage form , or for functional food applications, on its own or in combination with biologically active compounds. It may also be used as a supplement in fish feed microparticles. Typically, the composition is a free flowing powder.
- the deoiled MPL powder may be further processed and purified using e.g. ethanol extraction to remove t the phospholipids and leave behind proteins, amino acids and most minerals as by products.
- ethanol e.g. ethanol extraction
- other solvents such as methanol, isopropanol, tert- butanol and n-propanol are equally suitable.
- the composition is a waxy, paste like material and comprises a purified MPL composition containing 70 wt% to 95 wt% (or more after column chroatography) of phospholipids, preferably above 75 wt% with a rrummum PC content of 40 wt%, preferably between 60 wt% to 80 wt% as the major component.
- About 30 wt% , preferably above 40 wt% of the esterified fatty acids in the PC comprise HUFAs.
- the HUFAs comprise between 40 wt% to 60 wt% of the omega- 3 fatty acids EPA and DHA.
- phospholipid types and typical amounts present are, PE (15 wt%), PI (10 wt%), SPM (5 wt%), PS (2 wt%) and their mono acyl derivatives (4 wt%). Also smaller amounts of glycolipids may be present.
- the non polar (neutral) lipids total 5 wt% to 30 wt% of the waxy MPL composition, preferably below 15 wt%.
- the maximum amount of cholesterol and cholesterol esters is about 8 wt%, preferably below 5 wt%.
- the phospholipid values are based on phosphorous- 31 NMR determinations. This purified composition may also be used for preparing the MPL concentrates in a Hquid form.
- PC enriched MPL having between 60 wt% to 95 wt% PC.
- Aluminium oxide is the material of choice if higher than 80 % PC concentration is desired.
- MPL compositions provide the desired fatty acid profiles and also allow maximum containment and delivery of nutritional components in a suitable form.
- the idea behind this invention is to exploit the intrinsic properties of particular types of marine phosphoHpid in compositions which are nutritionally beneficial and furthermore have the capacity to contain nutritional and other components by association/ complex formation.
- Factors to be considered in using a particulate MPL composition as nutritional supplement and food additive for human use are, i) between 70 wt% to 95 wt% of phospholipids in the lipid fraction which contain 10 wt% to 30 wt% of total Hpids, u) phosphatidylcholine content more than 40 wt% , preferably more than 60 wt% of the phosphoHpids with at least 30 wt% of HUFAs, wherein the fatty acid profiles provide desired levels of DHA and EPA, iii) low amounts of neutral Hpids, preferably below 15 wt%, iv) low in cholesterol and cholesterol esters, preferably below 5 %, iv) suitability as solid and conversion to Hquid unit dosage forms.
- MPL in feed particles v) avoidance of elevated temperatures and intensive mixing which may be deleterious in preparing concentrates that form lipid aggregates in water, vi) avoidance of organic solvents particularly ethanol which are commonly employed in (v) to solubiHse phospholipids.
- the invention provides ready to use marine phospholipid (MPL) compositions suitable for human or aquaculture appHcations which may be a dry composition comprising nutritional components selected from the group consisting of marine phosphoHpids, marine proteins and amino acid blends obtainable by fluid extraction of a dried marine raw material with less than 50 wt% water, preferably less than 10 wt%.
- MPL marine phospholipid
- a typical particulate composition prepared by fluid or supercritical gas extraction of the dry marine raw material comprises:
- Protein and amino acids 70 wt% to 90wt%
- Polar Hpids 70 wt% to 95 wt%
- PC content 40 wt% to 80 wt% (of polar Hpids) esterified HUFAs: 30 wt% to 40 wt% (of polar Hpids)
- Neutral (non polar) lipids 5 wt% to 20 wt% cholesterol, cholesterol esters: . ⁇ 8 wt% free fatty acids: ⁇ 5 wt%
- the invention also describes a method to prepare a purified, waxy marine phospholipid composition from a phosphoHpid/ marine protein/ arnino acid blend after acetone or more preferably supercritical gas treatment of a dried marine raw material, suitable for direct human consumption or other appHcations, obtainable by extraction of the phospholipids using solvents such as ethanol, methanol, isoproyl alcohol, tert-butanol and n-propyl alcohol, and mixtures thereof.
- solvents such as ethanol, methanol, isoproyl alcohol, tert-butanol and n-propyl alcohol, and mixtures thereof.
- the compositon obtained is a purified, waxy marine phospholipid mixture with low amounts of neutral Hpids suitable for preparing a water dispersible concentrate.
- the waxy composition may also be blended or mixed with a neutral oil to prepare a liquid or gel like Hpophilic composition which may be used in hard or soft gelatine capsules or the like for human nutritional purposes.
- the oil may be any physiologically acceptable neutral oil. Preferably it is a fish or a vegetable oil or it may be a medium chain triglyceri.de such as Miglyol and edible fatty acid esters, ethers.
- the amount of oil for blending may be between 25 wt% to 60 wt% or more depending on the purpose.
- the oil may simply be a diluent or it may be used as a supplement of unsaturated omega-6 fatty acids.
- the waxy MPL composition comprises about 70wt% to about 95 wt% or more of phosphoHpids comprising at least 40 wt% phosphatidylcholine calculated on the basis of the total phosphoHpids present which comprise about 30% by weight of esterfied omega-3 fatty- acids and between 5 wt% to 30 wt% of neutral Hpids.
- the purified phospholipid mixture may be preferred for preparing a water dispersible marine phosphoHpid (MPL) concentrate suitable for embedment in fish feed microparticles or as supplements of highly bioavailable long chain omega-3 fatty acids for human, animal and aquaculture use.
- a typical specification of the purified, waxy MPL composition prepared by the method described in this invention comprises:
- Polar Hpids 70 wt% to 95 wt%
- PC content 40 wt% to 80 wt% esterified HUFAs: 30 wt% to 40 wt% of polar Hpids non polar (neutral) Hpids: 5.0 wt% to 30 wt% cholesterol, cholesterol esters: ⁇ 8 wt% free fatty acids: ⁇ 5 wt%
- Iodine value 110 -130 ethanol: ⁇ 2.5 wt% rninerals,trace elements (ash): ⁇ 2 wt% water: ⁇ 5 wt%
- the invention describes a homogeneous water dispersible MPL concentrate which comprises: i) 25 wt% to 75 wt% of a MPL composition comprising PC or blend of PC and the monoacyl derivative prepared by enzyme hydrolysis in an amount of at least 40 wt% as the major component and minor amounts of other components including PE, PI,
- optionaUy other additives selected from the group consisting of polymers, nutritional components, stabiHsers, preservatives, and antioxidants.
- the water dispersible concentrate may be utilised in food for human nutrition, or as a supplement administered in a suitable unit dosage form with or without biologically active compounds. It may also be used to prepare Hpid aggregates embedded in feed particles to contain nutritional components for feeding fish Hvestock or fish larvae.
- the water dispersible concentrate is prepared using a purified, waxy phosphoHpid composition with at least 40 % by weight of PC purified by ethanol extraction of a particulate or powdered marine phosphoHpid/ marine protein, amino acid and minerals composition.
- the invention further describes a method to prepare a water dispersible MPL concentrate from MPL compositions obtained by fluid and ethanol extraction.
- the invention further provides a method of preparing Hpid aggregates which involves dispersing a lipid concentrate (B) comprising: i) 25 wt% to 75 wt% of an MPL composition comprising PC or blend of PC and the monoacyl derivative prepared by enzyme hydrolysis in an amount of at least 40 wt% as the major component and minor amounts of other components, including PE, PI,
- SPM, PS and their monoacyl derivatives ii) 15 wt% to 75 wt% of glycerol or another polyol, or sugar iii) 1 wt% to 50 wt% water, iv) optionaUy, other additives selected form the group consisting of polymers, nutritional components, stabiHsers, preservatives, and antioxidants; in water or an aqueous medium for embedment and inclusion in feed particles or addition to food for human consumption.
- the fatty acid profile of the phosphoHpids is characterised by at least 30 wt% of HUFAs, chiefly DHA and EPA based on the total fatty acid content present. Preferably it should comprise between 40 wt% and 60 wt% omega-3 fatty acids. Hydrophilic medium
- Suitable hydrophiHc medium are non toxic polyols such as glycerol, propylene glycol, polyglycerols and mixtures thereof.
- the preferred polyol is glyceroLFor human use ethanol may be suitable.
- Alternative polyols which may be used in place of or in addition to glycerol are aqueous sugar solutions comprising at least 25 wt% of e.g, glucose, sucrose, soluble maltodextrins, or polyhydric alcohols Hke mannitol and sorbitol etc.
- Natural gums particularly sodium alginates which can cross link with Ca++ ions are preferred as matrix forming material for the microparticles.
- Alternative materials are proteins such as gelatine, poly peptides and peptides such as casein and soya proteins.
- buffers include buffers, osmotic components, antioxidants and anti microbials commonly used in fish feeds and supplements.
- a purified, waxy MPL composition after ethanol reatment is hydrated in the hydrophiHc medium, preferably without using elevated temperatures to prepare a homogeneous water dispersible gel like concentrate.
- permitted antioxidants and preservatives may be added.
- the concentrates readily disperse into a variety of lipid aggregates below 10 ⁇ average diameter, preferably below l ⁇ measured by laser light diffraction.
- the concentrate further comprising nutritional components and alginates may be embedded in micro particle feed compositions.
- the amount of MPL concentrate that may be incorporated and embedded in the multicomponent feed composition may be between 10 wt% to 75 wt%, preferably 20 wt% to 40 wt%.
- the invention also includes MPL compositions wherein the mixture comprises marine diacyl phosphoHpids and their monoacyl derivatives.
- the mixture is prepared by enzyme hydrolysis using phosphoHpase A2 or Al on a phospholipid substrate which may be either a particulate MPL composition or a waxy composition according to the method described in EP 1011634.
- the amount of diacyl phosphoHpid to monoacy phosphoHpid in the enzyme hydrolysed MPL composition may be between 1:10 to 20:1.
- MPL compositions which may be used either as such in powder form or for preparing purified waxy lipid compositions which may be used to prepare improved water dispersible MPL concentrates, as nutritional supplements and/ or ingredients for functional foods as weH as the delivery and containment of nutritional components in multicomponent fish feed compositions.
- the MPL compositions in powder form and as water dispersible concentrates may be used in unit dosage forms as supplements to supply highly bioavailable omega-3 fatty acids for human use.
- the dosage forms may also contain biologicaHy active compounds in combination with the MPL compositions.
- MPL concentrates comprising standardised and clearly defined phosphoHpids for embedment in feed microparticles, which are nutritionauy essential in larvae feed.
- a dried marine raw material consisting 1000 g of freeze dried capelin roe with a total lipid content of 35 wt% is extracted in a batch extraction vessel with 40 kg/h carbon dioxide at 300 bar and 40° C for 4 hours to remove 180 g of a clear orange-brown oil containing 18 wt% of cholesterol and cholesterol esters.
- the particulate MPL composition in the form of a coarse powder which is recovered contains a total Hpid content of about 21 wt% , of which the major proportion (about 17 wt%) is polar phosphoHpids and 4 wt% are neutral lipids.
- About 70 wt% of the phosphoHpids is phosphatidylcholine comprising at least 30 wt% HUFAS.
- the composition is proteinaceous material including about 8 wt% minerals and trace elements.
- the composition has a mild fishy taste and odour with a peroxide value below 3 and may be used as such or mixed with suitable excipients in functional food appHcations.
- a unit dose of 300 mg of the powder may be filled into hard gelatine capsules for oral use as nutritional supplement.
- the powder may also be converted into tablets.
- the MPL composition may contain biologicaHy active compounds
- herring or cod roe may be used.
- An alternative dried starting material that may be used in this example is from krill.
- a typical purified composition comprises:
- PC content 72 wt% esterfied HUFAs: 33 wt% (of PC based on total Hpids) non polar (neutral) lipids: 13 wt% free fatty acids: 5 wt%
- the MPL composition may be blended with 50 wt% of an oil which may be a fish oil, vegetable oil or medium chain glyceride such as Miglyol, to prepare a fluid HpophiHc composition. Alternatively, it may also be hydrated overnight in glycerol at room temperature to prepare a hydophlic composition .
- the Hquid compositions may be filled into soft gelatine capsules for oral use or it may be used in fish and larvae feeds as in Example 1.
- the MPL is hydrated overnight in a solution of glycerol at room temperature to prepare a viscous gel like MPL concentrate.
- the MPL concentrate from Example 3 is mixed with up to 25 wt% HpophiHc nutritional components which may be fish triglycerides and anti oxidants such as Vit E, ascorbyl palmitate., t-butylated hydroxytoluene, t-butylated hydroxyanisole, ascorbic acid or ethoxyquin. Additionally 25 wt% to 50 wt% of hydrophiHc fish feed components such as fish protein hydrolysates may be added. 2 wt% sodium alginate in aqueous solution may be added to the MPL concentrate as shown in the example.
- the resultant aqueous suspension of Hpid aggregates associated with nutritional components and alginate is used to prepare feed microparticles by cross linking the alginate in the composition in a bath containing Ca ++ ions to prepare microparticles as described in WO0027218.
- the microparticles are recovered and dried.
- a typical composition is illustrated below.
- Glycerol 70 %) 10.0 wt% Water (containing 2% Sod alginate) 19.5 wt%
- waxy MPL composition with a mininiun PC content of about 40 wt% may also be used.
- marine phospholipids (MPL) compositions suitable for human, feed and aquaculture purposes comprising a dry composition comprising nutritional components selected from the group consisting of marine phospholipids, marine proteins and amino acid blends obtainable by fluid extraction of a dried marine raw material.
- the compositions have low amounts of neutral Hpids and particularly low amounts of cholesterol and cholesterol esters. They may be used either as such in powder form and for preparing purified MPL compositions by ethanol extraction. Both forms may be used as nutritional supplements, ingredients for functional foods either on their own or in combination with biologically active compounds and to optimise the deHvery and containment of nutritional components in multicomponent fish feed compositions.
- MPL concentrates comprising purified and clearly defined phospholipid types dispersed in hydrophiHc medium which are nutritionaUy essential in larvae feed.
- StiU further there is described MPL concentrates in unit dosage forms as supplements to supply highly bioavaHable omega-3 fatty acids for human use, optionaUy with biologicaUy active compounds.
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Abstract
Description
Claims
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002507243A CA2507243A1 (en) | 2002-11-26 | 2003-11-26 | Marine lipid compositions |
| EP03775394A EP1569525A1 (en) | 2002-11-26 | 2003-11-26 | Marine lipid compositions |
| JP2005510238A JP2006507846A (en) | 2002-11-26 | 2003-11-26 | Marine phospholipid composition |
| AU2003283429A AU2003283429A1 (en) | 2002-11-26 | 2003-11-26 | Marine lipid compositions |
| US10/536,450 US20060128665A1 (en) | 2002-11-26 | 2003-11-26 | Marine lipid compositions |
| NO20052498A NO20052498L (en) | 2002-11-26 | 2005-05-24 | Marine Lipid Compounds |
| IS7861A IS7861A (en) | 2002-11-26 | 2005-05-24 | Marine lipid formulations |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP02258116 | 2002-11-26 | ||
| EP02258116.9 | 2002-11-26 | ||
| EP03255278 | 2003-08-25 | ||
| EP03255278.8 | 2003-08-25 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2004047554A1 true WO2004047554A1 (en) | 2004-06-10 |
Family
ID=32395462
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2003/013299 Ceased WO2004047554A1 (en) | 2002-11-26 | 2003-11-26 | Marine lipid compositions |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20060128665A1 (en) |
| EP (1) | EP1569525A1 (en) |
| JP (1) | JP2006507846A (en) |
| AU (1) | AU2003283429A1 (en) |
| CA (1) | CA2507243A1 (en) |
| IS (1) | IS7861A (en) |
| NO (1) | NO20052498L (en) |
| WO (1) | WO2004047554A1 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2006054183A3 (en) * | 2004-11-17 | 2006-08-31 | Natural Asa | Enzymatically synthesized marine phospholipids |
| WO2007123425A1 (en) * | 2006-04-20 | 2007-11-01 | David Stevenson | Process for separating lipid materials |
| WO2008060163A1 (en) * | 2006-11-16 | 2008-05-22 | Pronova Biopharma Norge As | Process for production of omega-3 rich marine phospholipids from krill |
| WO2008050219A3 (en) * | 2006-10-24 | 2008-06-19 | Krill As | Method and equipment' for improved extraction of lipid fractions from aquatic animals and from marine origin |
| WO2010097699A1 (en) * | 2009-02-26 | 2010-09-02 | Aker Biomarine Asa | Phospholipid and protein tablets |
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| WO2014120099A1 (en) * | 2013-01-29 | 2014-08-07 | Guetari Sami | Improved omega-3 food supplement based on marine oil |
| US8829215B2 (en) | 2008-05-15 | 2014-09-09 | Pronova Biopharma Norge As | Krill oil process |
| US8846604B2 (en) | 2011-09-02 | 2014-09-30 | Artic Nutrition AS | Lipid compositions with high DHA content |
| US9028877B2 (en) | 2007-03-28 | 2015-05-12 | Aker Biomarine Antarctic As | Bioeffective krill oil compositions |
| WO2016055860A1 (en) * | 2014-10-10 | 2016-04-14 | Enzymotec Ltd. | Marine lecithin preparations with enhanced oxidation resistance |
| EP2275140B1 (en) * | 2004-07-19 | 2017-11-01 | Bergen Teknologioverforing AS | Composition comprising plant and/or fish oils and non-oxidizable fatty acid entities |
| US9867856B2 (en) | 2014-01-10 | 2018-01-16 | Aker Biomarine Antarctic As | Phospholipid compositions and their preparation |
| US10456412B2 (en) | 2015-02-11 | 2019-10-29 | Aker Biomarine Antarctic As | Lipid extraction processes |
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| US10864223B2 (en) | 2015-02-11 | 2020-12-15 | Aker Biomarine Antarctic As | Lipid compositions |
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| CA2920789C (en) | 2015-06-04 | 2021-05-18 | Advance International, Inc. | Improved methods and systems for recovering protein powder and natural omega-3 oil from animal tissue |
| US11730782B2 (en) | 2020-11-20 | 2023-08-22 | Nooter/Eriksen, Inc | Processes for producing omega-3 containing compositions from algae and related extractions |
| AU2022452900A1 (en) * | 2022-04-11 | 2024-10-10 | Nooter/Eriksen, Inc. | Improved processes for producing omega-3 containing compositions from algae and related extractions |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1175486A1 (en) * | 1983-08-31 | 1985-08-30 | Ордена Трудового Красного Знамени Институт Биохимии Им.А.В.Палладина | Method of obtaining a complex of phospholipides |
| JPS6256497A (en) * | 1985-09-05 | 1987-03-12 | Nisshin Oil Mills Ltd:The | Production of phospholipid composition containing eicosapentaenoic acid |
| JPH02215351A (en) * | 1989-02-14 | 1990-08-28 | Taiyo Fishery Co Ltd | Method for collecting krill phospholipid and functional food and nerve function improving agent having nerve function improving effect |
| JPH06212186A (en) * | 1992-05-28 | 1994-08-02 | Agency Of Ind Science & Technol | Production of eicosapentaenoic acid from red alga fudaraku |
| US5434183A (en) * | 1991-05-30 | 1995-07-18 | Pharmacia Ab | Phospholipids containing omega-3-fatty acids |
| JPH09194362A (en) * | 1996-01-19 | 1997-07-29 | Bizen Kasei Kk | Composition consisting of phospholipid containing docosahexanenoic acid and eicosapentanenoic acid |
| WO2001050884A1 (en) * | 2000-01-14 | 2001-07-19 | Baldur Hjaltason | Marine lipid composition for feeding aquatic organisms |
| US6372460B1 (en) * | 1997-08-01 | 2002-04-16 | Martek Biosciences | DHA-containing nutritional compositions and methods for their production |
| WO2002092540A1 (en) * | 2001-05-14 | 2002-11-21 | Martek Biosciences Corporation | Production and use of a polar lipid-rich fraction containing omega-3 and/or omega-6 highly unsatruated fatty acids from microbes, genetically modified plant seeds and marine organisms |
-
2003
- 2003-11-26 EP EP03775394A patent/EP1569525A1/en not_active Withdrawn
- 2003-11-26 WO PCT/EP2003/013299 patent/WO2004047554A1/en not_active Ceased
- 2003-11-26 CA CA002507243A patent/CA2507243A1/en not_active Abandoned
- 2003-11-26 US US10/536,450 patent/US20060128665A1/en not_active Abandoned
- 2003-11-26 AU AU2003283429A patent/AU2003283429A1/en not_active Abandoned
- 2003-11-26 JP JP2005510238A patent/JP2006507846A/en not_active Withdrawn
-
2005
- 2005-05-24 IS IS7861A patent/IS7861A/en unknown
- 2005-05-24 NO NO20052498A patent/NO20052498L/en not_active Application Discontinuation
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1175486A1 (en) * | 1983-08-31 | 1985-08-30 | Ордена Трудового Красного Знамени Институт Биохимии Им.А.В.Палладина | Method of obtaining a complex of phospholipides |
| JPS6256497A (en) * | 1985-09-05 | 1987-03-12 | Nisshin Oil Mills Ltd:The | Production of phospholipid composition containing eicosapentaenoic acid |
| JPH02215351A (en) * | 1989-02-14 | 1990-08-28 | Taiyo Fishery Co Ltd | Method for collecting krill phospholipid and functional food and nerve function improving agent having nerve function improving effect |
| US5434183A (en) * | 1991-05-30 | 1995-07-18 | Pharmacia Ab | Phospholipids containing omega-3-fatty acids |
| JPH06212186A (en) * | 1992-05-28 | 1994-08-02 | Agency Of Ind Science & Technol | Production of eicosapentaenoic acid from red alga fudaraku |
| JPH09194362A (en) * | 1996-01-19 | 1997-07-29 | Bizen Kasei Kk | Composition consisting of phospholipid containing docosahexanenoic acid and eicosapentanenoic acid |
| US6372460B1 (en) * | 1997-08-01 | 2002-04-16 | Martek Biosciences | DHA-containing nutritional compositions and methods for their production |
| WO2001050884A1 (en) * | 2000-01-14 | 2001-07-19 | Baldur Hjaltason | Marine lipid composition for feeding aquatic organisms |
| WO2002092540A1 (en) * | 2001-05-14 | 2002-11-21 | Martek Biosciences Corporation | Production and use of a polar lipid-rich fraction containing omega-3 and/or omega-6 highly unsatruated fatty acids from microbes, genetically modified plant seeds and marine organisms |
Non-Patent Citations (6)
| Title |
|---|
| DATABASE WPI Section Ch Week 198611, Derwent World Patents Index; Class B05, AN 1986-074743, XP002276083 * |
| DATABASE WPI Section Ch Week 198716, Derwent World Patents Index; Class B05, AN 1987-111742, XP002276086 * |
| DATABASE WPI Section Ch Week 199040, Derwent World Patents Index; Class B04, AN 1990-302732, XP002276087 * |
| DATABASE WPI Section Ch Week 199435, Derwent World Patents Index; Class B05, AN 1994-283548, XP002276084 * |
| DATABASE WPI Section Ch Week 199740, Derwent World Patents Index; Class B05, AN 1997-431382, XP002276085 * |
| PATENT ABSTRACTS OF JAPAN vol. 014, no. 513 (C - 0777) 9 November 1990 (1990-11-09) * |
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| US9867856B2 (en) | 2014-01-10 | 2018-01-16 | Aker Biomarine Antarctic As | Phospholipid compositions and their preparation |
| CN107105695A (en) * | 2014-10-10 | 2017-08-29 | 恩兹莫特克有限公司 | Ocean lecithin preparations with enhanced inoxidizability |
| WO2016055860A1 (en) * | 2014-10-10 | 2016-04-14 | Enzymotec Ltd. | Marine lecithin preparations with enhanced oxidation resistance |
| US10456412B2 (en) | 2015-02-11 | 2019-10-29 | Aker Biomarine Antarctic As | Lipid extraction processes |
| US10864223B2 (en) | 2015-02-11 | 2020-12-15 | Aker Biomarine Antarctic As | Lipid compositions |
| US11819509B2 (en) | 2015-02-11 | 2023-11-21 | Aker Biomarine Antarctic As | Lipid compositions |
Also Published As
| Publication number | Publication date |
|---|---|
| IS7861A (en) | 2005-05-24 |
| CA2507243A1 (en) | 2004-06-10 |
| EP1569525A1 (en) | 2005-09-07 |
| NO20052498L (en) | 2005-08-26 |
| NO20052498D0 (en) | 2005-05-24 |
| US20060128665A1 (en) | 2006-06-15 |
| AU2003283429A1 (en) | 2004-06-18 |
| JP2006507846A (en) | 2006-03-09 |
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