WO2021156385A1 - Lipid composition comprising omega-3 fatty acids - Google Patents

Lipid composition comprising omega-3 fatty acids Download PDF

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Publication number
WO2021156385A1
WO2021156385A1 PCT/EP2021/052702 EP2021052702W WO2021156385A1 WO 2021156385 A1 WO2021156385 A1 WO 2021156385A1 EP 2021052702 W EP2021052702 W EP 2021052702W WO 2021156385 A1 WO2021156385 A1 WO 2021156385A1
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Prior art keywords
lipid composition
fatty acid
ethyl esters
acid ethyl
composition
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PCT/EP2021/052702
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French (fr)
Inventor
Andreas Alfred WEBER
Jennifer Jung
Frantz Sylvain DESCHAMPS
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Wellness Holding B.V.
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Publication of WO2021156385A1 publication Critical patent/WO2021156385A1/en

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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/4841Filling excipients; Inactive ingredients
    • A61K9/4858Organic compounds
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23DEDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/007Other edible oils or fats, e.g. shortenings, cooking oils characterised by ingredients other than fatty acid triglycerides
    • A23D9/013Other fatty acid esters, e.g. phosphatides
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23JPROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J7/00Phosphatide compositions for foodstuffs, e.g. lecithin
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L33/00Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/115Fatty acids or derivatives thereof; Fats or oils
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/48Preparations in capsules, e.g. of gelatin, of chocolate
    • A61K9/4841Filling excipients; Inactive ingredients
    • A61K9/4875Compounds of unknown constitution, e.g. material from plants or animals
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

Definitions

  • the invention relates to a pourable lipid composition
  • a pourable lipid composition comprising: a) lecithin component selected from glycerophospholipids, glycolipids and combinations thereof; b) fatty acid ethyl esters comprising ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid, docosahexaenoic acid and combinations thereof; c) partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; and d) optionally, triacylglycerides.
  • the invention also provides an oral dosage unit comprising the aforementioned lipid composition and a process for the manufacture of said lipid composition.
  • Omega-3 fatty acids also called w-3 fatty acids or n-3 fatty acids, are polyunsaturated fatty acids (PUFAs) characterized by the presence of a double bond three atoms away from the terminal methyl group in their chemical structure.
  • the three main naturally occurring omega- 3 fatty acids are alpha-linolenic acid (ALA), eicosapentaenoic acid (EPA), and docosahexaenoic acid (DHA).
  • ALA alpha-linolenic acid
  • EPA eicosapentaenoic acid
  • DHA docosahexaenoic acid
  • ALA is found mainly in plant oils such as flaxseed, soybean, and canola oils.
  • Sources of EPA and DHA include fish, fish oils, eggs from chickens fed EPA and DHA, squid oils, krill oil, and certain algae.
  • EPA acts as a precursor for prostaglandin-3 (which inhibits platelet aggregation), thromboxane-3, and leukotriene-5 eicosanoids.
  • Vascepa ethyl eicosapentaenoic acid
  • EPA a prescription drug containing only EPA
  • DHA is a major fatty acid in brain phospholipids and the retina.
  • the potential roles of DHA in the mechanisms of Alzheimer's disease are under active research.
  • the European Food Safety Authority has approved health claims on omega-3 fatty acids. DHA/EPA for maintenance of normal cardiac function and normal (fasting) blood concentrations of triglycerides. DHA for maintenance of normal vision and normal brain function.
  • omega-3 oils from these sources are deemed to be superior to omega-3 oils from plant sources, notably algae.
  • Krill oil in particular is regarded as an excellent source of EPA and DHA. This is because krill oil, besides providing high levels of EPA and DHA, also provides the following favourable nutritional attributes:
  • phospholipids - EPA and DHA in krill oil are more efficiently absorbed by the human body as they are largely contained in phospholipids, whereas in other sources, such as fish oil, these omega-3 fatty acids are contained in triglycerides, which are insoluble and require bile salts for their emulsification and absorption via the lymphatic system.
  • Krill oil is an extract prepared from a species of Antarctic krill, Euphausia superba.
  • Krill oil is characterized by a high glycerophospholipid content, phosphatidylcholine representing the bulk of the glycerophospholipids.
  • krill oil contains triglycerides, diglycerides, monoglycerides and free fatty acids.
  • Phospholipids typically represent 40-80 wt.% of the lipids contained in krill oil.
  • Krill oils as well as fish oils have the drawback that there are concerns regarding sustainability. Furthermore, supplements based on these animal oil are not suited for vegetarians and vegans.
  • US 2017/0182074 describes a liquid composition having a viscosity of less than 3000 mPa.s when measured at a temperature within the range 25-70°C, wherein the composition comprises (i) at least 80% by weight of a phospholipid-containing krill extract which has a viscosity of at least 3000 mPa.s when measured at a temperature where the liquid composition has a viscosity of less than 3000 mPa-s and (ii) no more than 20% by weight of a viscosity-reducing agent.
  • Suitable viscosity-reducing agents include lower alcohols, benzyl alcohol, glycerol, and glycols (e.g.
  • the US patent application also describes an oral capsule for human use including an encapsulated liquid composition, wherein (a) the capsule is made from a material which includes glycerol, and (b) the liquid composition comprises purified krill phospholipids and glycerol.
  • CN 104306383 describes a soft capsule comprising phospholipid and unsaturated fatty acid ester.
  • Example 1 describes the preparation of a capsule comprising a mixture of 65 parts by weight of phospholipid and 35 parts by weight of unsaturated fatty acid ester.
  • CN 108265090 describes a method or preparing an fat or oil composition containing almost the same phospholipid-type DHA and phospholipid-type EPA as natural Antarctic krill oil.
  • This fat or oil composition is prepared by transesterification of soybean lecithin with ethyl ester of EPA and ethyl ester of DHA.
  • Lipoid GmbH (“Water soluble composition containing omega-3-fatty acids for use in dietetics and food', Research Disclosure, Kenneth Mason Publications, Hampshire, UK, vol. 527, no. 13) relates to water soluble compositions comprising omega-3 fatty acids.
  • WO 2013/072767 relates to compositions comprising:
  • a fatty acid oil mixture comprising EPA and DHA, wherein the EPA and DHA are in a form chosen from free fatty acid, ethyl ester, triglyceride and phospholipid, and
  • WO 2008/068276 relates to soft gelatin capsules containing a liquid or pasty lipophilic phase and aspirin.
  • WO 2015/142705 relates to dietary supplement compositions comprising an algae based oil having glycolipids and phospholipids and EPA fatty acids in combination with astaxanthin and hyaluronic acid or sodium hyaluronate.
  • the present invention relates to a pourable lipid composition that provides very high levels of EPA and/or DHA in highly bioavailable form and that provides a suitable alternative for krill oil. More particularly, the invention relates to a pourable lipid composition comprising the following components:
  • lecithin component selected from glycerophospholipids, glycolipids and combinations thereof, including at least 20 wt.%, calculated by weight of the lipid composition, of glycerophospholipids;
  • (d) 0-30 wt.% triacylglycerides; wherein the lecithin component and the fatty acid ethyl esters are contained in the lipid composition in a weight ratio of less than 1.5:1; wherein the fatty acid ethyl esters comprise at least 35 wt.% of ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid, docosahexaenoic acid and combinations thereof; wherein the combination of components (a), (b), (c) and (d) comprises at least 90 wt.% of the composition; and wherein the combination of components (a) and (b) comprises at least 65 wt.% of the composition.
  • the pourable lipid composition of the present invention can suitably be manufactured using only lipids from plant sources, e.g. using omega-3 oil from algae and lecithin from soybean or rapeseed.
  • omega-3 oil can be converted into fatty acid ethyl esters by transesterification with ethanol.
  • the lipid composition of the present invention can be provided in a shelf-stable liquid form. Furthermore, the emulsifying action of the glycerophospholipids aids the absorption of the apolar fatty acid ethyl esters and thereby increases bioavailability of the omega-3 fatty acids.
  • the lipid composition of the present invention can contain high levels of EPA and/or DHA, allowing it to be used in supplements in the form of oral dosage units, such as capsules. Accordingly, the present invention also provides a dosage unit comprising 100-2000 mg of the aforementioned lipid composition.
  • lipid composition of the present invention comprising the steps: a) partially transesterifying algal oil with ethanol to produce a transesterified composition containing fatty acid ethyl ester and partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; b) combining the transesterified composition with lecithin.
  • This process offers the advantage that EPA and DHA containing ethyl esters and EPA and DHA containing partial glycerides are produced in one step.
  • the invention relates to the use of the present lipid composition in the treatment or prevention of cardiovascular-related disease, dry eye syndrome, Meibomian gland dysfunction, macular edema, Alzheimer’s disease and traumatic brain injury.
  • a first aspect of the present invention relates to a pourable lipid composition
  • a pourable lipid composition comprising the following components:
  • lecithin component selected from glycerophospholipids, glycolipids and combinations thereof, including at least 20 wt.%, calculated by weight of the lipid composition, of glycerophospholipids;
  • EPA eicosapentaenoic acid
  • DHA docosahexaenoic acid
  • liquid means that at 20 °C the lipid composition can be poured out a container.
  • glycolides refers to fatty acid esters of glycerol (triacylglycerides, diacylglycerides and monoacylglycerides).
  • fatty acid refers to a carboxylic acid with a long non-branched aliphatic chain of 6-24 carbon atoms.
  • glycophospholipids refers to derivatives of glycerophosphoric acid that contains at least one fatty acid residue attached to the glycerol moiety.
  • examples of glycerophospholipids include phosphatidylcholine (PC), phosphatidylethanolamine (PE), phosphatidylinositol (PI), phosphatidylserine (PS) and phosphatidic acid (PA).
  • glycolipid refers a monosaccharide or oligosaccharide bound to a lipid moiety by means of a glycosidic bond.
  • Fatty acid concentrations as referred to herein, unless indicated otherwise, relate to the percentage by weight (% w/w) of the total combined amount of free fatty acids and fatty acid residues.
  • the combination of components (a)) and (b) preferably comprises at least 75wt.%, more preferably at least 85 wt.% and most preferably at least 90 wt.% of the present lipid composition.
  • the combination of components (a), (b), (c) and (d) preferably comprises at least 92 wt.%, more preferably at least 93 wt.% and most preferably at least 94 wt.% of the lipid composition.
  • all the components a) to d) of the lipid composition are plant derived.
  • the entire lipid composition is plant derived.
  • the lipid composition of the present invention preferably provided at least 150 mg/g, more preferably 180-500 mg/g and most preferably 200-350 mg/g of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
  • the lipid composition provides 12-80 mg/g, more preferably 18-70 mg/g and most preferably 24-65 mg/g alpha-linolenic acid (ALA).
  • ALA alpha-linolenic acid
  • the lipid composition of the present invention preferably comprises 33-58 wt.% lecithin component, more preferably 35-56 wt.% lecithin component, and most preferably 36-52 wt.% lecithin component.
  • the lipid composition of the present invention preferably comprises 25-50 wt.% glycerophospholipids, more preferably 27-45 wt.% glycerophospholipids, and most preferably 28-40 wt.% glycerophospholipids.
  • the lecithin component is obtained from soybean and/or rapeseed as the glycerophospholipids of these plant sources contain significant levels of omega-3 fatty acid residues in the form of alpha-linolenic acid.
  • Preferably 2-15 wt.%, more preferably 3-12 wt.% and most preferably 4-9 wt.% of the fatty acid residues in the glycerophospholipids is alpha-linolenic acid residue (ALA).
  • ALA alpha-linolenic acid residue
  • the glycerophospholipids of the present invention typically do not contain more than a limited amount of EPA and/or DHA. Accordingly, in a preferred embodiment, 0-10 wt.%, more preferably 0-5 wt.% and most preferably 0-3 wt.% of the fatty acid residues in the glycerophospholipids are omega-3 fatty acids selected from EPA, DHA and combinations thereof. Unsaturated fatty acid residues preferably constitute at least 75 wt.%, more preferably at least 80 wt.% and most preferably at least 85 wt.% of the fatty acid residues in the glycerophospholipids.
  • Polyunsaturated fatty acid residues preferably constitute at least 25 wt.%, more preferably at least 28 wt.% and most preferably at least 30 wt.% of the fatty acid residues in the glycerophospholipids.
  • the glycerophospholipids in the lipid composition preferably comprise at least 10 wt.% phosphatidylcholine, more preferably 20-80 wt.% phosphatidylcholine, most preferably 30-60 wt.% phosphatidylcholine.
  • the glycerophospholipids in the lipid composition preferably comprise at least 5 wt.% phosphatidylethanolamine, more preferably 10-50 wt.% phosphatidylethanolamine, most preferably 20-35 wt.% phosphatidylethanolamine.
  • the lipid composition preferably comprises 35-66 wt.% fatty acid ethyl esters, more preferably 38-64 wt.% fatty acid ethyl esters and most preferably 40-63 wt.% fatty acid ethyl esters.
  • the fatty acid ethyl esters comprise 0.5-30 wt.% eicosapentaenoic acid ethyl esters, more preferably 3-20 wt.% eicosapentaenoic acid ethyl esters, most preferably 5-15 wt.% eicosapentaenoic acid ethyl esters.
  • the fatty acid ethyl esters comprise 30-60 wt.% docosahexaenoic acid ethyl esters, more preferably 32-50 wt.% docosahexaenoic acid ethyl esters, most preferably 35-40 wt.% docosahexaenoic acid ethyl esters.
  • eicosapentaenoic acid ethyl esters and docosahexaenoic acid ethyl esters together constitute at least 30 wt.% , more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid ethyl esters in the lipid composition.
  • the lipid composition preferably comprises partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof. Partial glycerides containing omega-3 fatty acids may be produced in the preparation of the ethyl esters of fatty acids by transesterification of triglycerides with ethanol or they can be produced separately by transesterification of omega-3 oil with glycerol.
  • the lipid composition preferably comprises 0.2-10 wt.%, more preferably 0.3-6 wt.% and most preferably 0.4-4 wt.% of the partial glycerides.
  • At least 30 wt.%, more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid residues in the partial glycerides are residues of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
  • Triacylglycerides are preferably comprised in the lipid composition in a concentration of 0.1- 20 wt.%, more preferably a concentration of 0.2-10 wt.% and most preferably in a concentration of 0.3-5 wt.%.
  • At least 35 wt.%, more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid residues in the triacylglycerides are residues of omega-3 fatty acids selected from EPA, DHA and combinations thereof
  • the ratio on a weight basis of the glycerophospholipids to the fatty acid ethyl esters in the lipid composition is preferably in the range of 1:3 to 1:1, more preferably in the range of 1:2.8 to 1:1.1, and most preferably in the range of 1:2.5 to 1:1.2.
  • the ratio on a weight basis of the partial glycerides to the triacylglycerides in the lipid composition is preferably at least 1:30, more preferably at least 1:20, and most preferably in the range of 1:15 to 3:1.
  • the lipid composition further comprises 0.001-1.5 wt.%, more preferably 0.1-1.2 wt.% and most preferably 0.3-0.9 wt.% carotenoids selected from beta carotene, lutein, astaxanthin, zeaxanthine.
  • the lipid composition comprises 1-2,000 ppm (mg/kg), more preferably 100-1,500 ppm, most preferably 300-900 ppm astaxanthin.
  • the lipid composition further comprises 0.01-2 wt.%, more preferably 0.1 -1.5 wt.% and most preferably 0.3-1 wt.% tocopherol.
  • the pourable lipid composition of the present invention preferably has a viscosity of not more than 10,000 cP, more preferably of 200 to 9000 cP at 20 °C and a shear rate of 100 s 1 .
  • the pourable lipid composition preferably shows less than 5 wt.%, more preferably less than 2 wt.% and most preferably less than 1 wt.% phase separation when the composition is kept in a sealed glass container at 20°C for 2 months.
  • the wt.% phase separation is determined gravimetrically after decantation.
  • Another aspect of the invention relates to an oral dosage unit comprising 100-2000 mg, more preferably comprising 300-1500 mg, most preferably comprising 400-1000 mg of the pourable lipid composition of the invention.
  • the oral dosage unit provides 150-500 mg, more preferably 200-400 mg and most preferably 250-350 mg of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
  • the oral dosage unit provides 10-100 mg, more preferably 15-80 mg and most preferably 20-50 mg ALA.
  • the oral dosage unit of the present invention preferably is a capsule that is filled with the pourable lipid composition.
  • the capsule comprises a gel film, more preferably a vegetarian gel film, i.e. a gel film that does not contain animal products such as gelatin.
  • the capsule comprising the gel film preferably has a water content in the range of 5 to 30 wt.%, more preferably of 8 to 25 wt.%, most preferably in the range of 10 to 22 wt.%.
  • the inventors have observed that water present in the capsule tends to migrate from the capsule towards the lipid composition, possibly due to the high phospholipid content of the lipid composition. This migration of water has an adverse effect on the capsule in that the corresponding lowering of the water content causes the gel film to become less elastic, brittle and fragile. At the same time, the increase in water content of the lipid composition can cause phase separation in the lipid composition, especially near the interface with the capsule.
  • polar liquids examples include water, ethyl lactate, glycerol, ethylene glycol, propylene glycol, polyethylene glycol and combinations thereof. More preferably, the polar liquid is selected from water, ethyl lactate and combinations thereof. Most preferably, the polar liquid is ethyl lactate.
  • the aforementioned polar liquid is preferably comprised in the pourable lipid composition in a concentration of 0.5-10 wt.%, more preferably in a concentration of 1-8 wt.% and most preferably in a concentration of 1.5-6 wt.%.
  • Yet another aspect of the invention relates to a process for the manufacture of a lipid composition as described herein before, said process comprising the steps: a) partially transesterifying algal oil with ethanol to produce a transesterified composition containing fatty acid ethyl ester and partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; b) combining the transesterified composition with lecithin.
  • the present process yields a pourable lipid composition as defined herein before.
  • the transesterified composition that is produced by the partial transesterification of algal oil preferably comprises 0.4-20 wt.%, more preferably 0.6-12 wt.% and most preferably 0.8-8 wt.% of the partial glycerides.
  • At least 30 wt.%, more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid residues in the algal are residues of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
  • the algal oil used as a staring material in the present process preferably comprises at least 25 wt.%, more preferably at least 50 wt.% and most preferably at least 80 wt.% triacylglycerides.
  • the algal oil employed in the present process preferably is an oil extracted from one or more of the genera Schizochytrium, Isochrysis, Nannochloris, Tetracelmis, Nannochloropsis, Chlorella. Most preferably, the algal oil is extracted from Schizochytrium.
  • the transesterification is catalysed by an ethoxide salt selected from lithium ethoxide, sodium ethoxide, potassium ethoxide, preferably the ethoxide salt is sodium ethoxide.
  • an ethoxide salt selected from lithium ethoxide, sodium ethoxide, potassium ethoxide, preferably the ethoxide salt is sodium ethoxide.
  • the transesterification is catalysed by a lipase.
  • the lecithin used in the present process is preferably selected from rapeseed lecithin, soy lecithin, sunflower lecithin, corn lecithin, cottonseed lecithin, sesame lecithin, perilla lecithin, linseed lecithin and combinations thereof. More preferably, the lecithin is selected from rapeseed lecithin, soy lecithin and combinations thereof.
  • the lecithin employed in the present process preferably has a glycerophospholipid content of at least 40 wt.%, more preferably of at least 55 wt.% and most preferably of 60-95 wt.%.
  • the ethanol and the algal oil are preferably combined in a weight ratio of 1:2 to 1:20, more preferably in a weight ratio of 1:2.5 to 1:16 and most preferably in a weight ratio of 1 :3 to 1 :6.
  • Any ethanol remaining in the transesterified composition is preferably removed before the composition is combined with the lecithin.
  • the transesterified composition and the lecithin are preferably combined in a weight ratio of 40:60 to 70:30, more preferably in a weight ratio of 42:58 to 68:32 and most preferably in a weight ratio of 45:55 to 65:35.
  • Yet another aspect of the present invention relates to the use of the lipid composition of the present invention or of the oral dosage unit of the present invention for use in the treatment or prevention of cardiovascular-related disease, dry eye syndrome, Meibomian gland dysfunction, macular edema Alzheimer’s disease and traumatic brain injury.
  • the lipid composition or oral dosage unit is used in the treatment or prevention of cardiovascular-related disease, more particularly a cardiovascular-related disease selected from high blood pressure, coronary heart disease, dyslipidemia, congestive heart failure and stroke.
  • said use comprises orally administering of the lipid composition or the oral dosage unit. More preferably, the use comprises oral administration to provide a dose of at least 500 mg, more preferably a dose of 600-2,000 mg and most preferably a dose of 750- 950 mg of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
  • Transesterified algae oil was prepared as follows. 100.3 g of omega-3 triglyceride oil from Schizochytrium sp. (DSM life’s Omega 60, 15% EPA 30% DHA) were warmed up to 50°C in a water bath under stirring and under nitrogen. 0.50 g of NaOH and 199.3 g of anhydrous ethanol were mixed at ambient temperature until complete dissolution. The ethanolic NaOH solution was added to the triglyceride oil. The mixture was initially cloudy but cleared after 1 min. The reaction was stopped after 5 min. The transesterified oil was mixed with 400 ml of hot tap water in a 1L-separating funnel which led to a stable, milky mixture. Sodium chloride was added to speed up phase separation. After two hours, both phases were still cloudy. The upper phase was washed a second time with 300 ml of demineralized water. The washed transesterified oil was filtered on a pleated filter to reduce its residual water amount.
  • DSM life Omega 60,
  • Powdered de-oiled rapeseed lecithin (98.5% acetone insolubles) was partially extracted with ethanol - water to obtain an extract rich in PC and PE and leaving a residue containing other complex and neutral lipids according to a method described by Patil et al. ( Extraction and purification of phosphatidylcholine from soyabean lecithin, Separation and Purification Technology 75 (2010) 138-144).
  • transesterified oil 48.8 g of transesterified oil were mixed with 29.8 g of refined lecithin in a beaker at 50° under stirring during 15 min.
  • the lipid composition so obtained had a very low, water-like viscosity and was stable under different storage conditions (room temperature, 4 °C in refrigerator) for days.
  • the composition of the lipid composition is shown in Table 1.
  • Transesterified algae oil was prepared as follows. 570.3 g of omega-3 triglyceride oil from Schizochytrium sp. (DSM life’s Omega 60, 15% EPA 30% DHA) were warmed up to 50°C in a 1 L stirred reactor on a water bath under nitrogen. 2.0 g of NaOH and 199.9 g of anhydrous ethanol were mixed at ambient temperature until complete dissolution. The NaOH ethanolic solution was added to the triglyceride oil. After 2 hours 300 g deionised water were added to stop the reaction and to wash out salts and other byproducts. The mixture was left to settle for 1 hour and 20 minutes and the water phase was withdrawn. The procedure was repeated with another 200 ml of deionised water and the water phase was again withdrawn after a settling time of 2 hours.
  • transesterified oil phase so obtained was mixed with 5 g micro-crystalline cellulose to bind residual water. After letting the cellulose settle overnight the oil was filtered over paper filter to yield 511.15g of transesterified algae oil.
  • the pourable lipid composition so obtained stayed homogeneous during several days at room temperature as well as at 4 °C in a refrigerator.
  • composition of the lipid composition is shown in Table 2.
  • Transesterified algae oil was prepared as follows. 10.04 kg of omega-3 triglyceride oil from Schizochytrium sp. (DSM life’s Omega 60, 15% EPA 30% DHA) were warmed up to 50°C in a 20 L stirred reactor with a heating jacket and recirculated water heater under nitrogen. 35.0 g of NaOH and 3.45 kg of anhydrous ethanol were mixed at ambient temperature until complete dissolution. After equilibrating the triglyceride oil at 50°C, the NaOH ethanolic solution was added to the oil by a dosage pump. After 2 hours of reaction 5 L deionised water were added to stop the reaction and to wash out salts and other byproducts.
  • the pourable lipid composition so obtained was filled into bottles and used for test runs for encapsulation into softgel capsules.
  • the composition of the lipid composition is shown in Table 3.
  • Vegetarian Softgel capsules were prepared containing 850 mg of the pourable composition of Example 3, using Vegesoft® capsules, supplied by Eurocaps, Tredegar, South Wales, NP224EF, United Kingdom..
  • Table 5 Pieces of Vegesoft® capsules (0.16 gram) were submerged in 15 grams of pourable lipid composition and left in there for three days. At the end of the storage time the pieces were removed from the lipid compositions, washed with hexane and allowed to dry. The weight of the pieces that had been stored in the different lipid compositions was compared with that of the original pieces. Also changes in the physical characteristics of the capsule materials and the lipid compositions were determined. The results are shown in Table 6.
  • the observed weight loss is believed to have been caused by migration of water of from the capsule material into the lipid composition, possibly triggered by the high phospholipid content of the lipid composition. Removal of water from the capsule material reduces the elasticity and renders the material more fragile. Migration of water into the pourable liquid compositions can cause destabilisation resulting in the formation of a viscous layer on the surface of the capsule material.
  • Transesterified algae oil was prepared using a two-fold excess of ethanol:
  • the transesterified algae oil contained 4 wt.% partial glycerides in the form of monoglycerides.
  • Lipid compositions were prepared by mixing the de-oiled rapeseed lecithin of Example 1 with the above mentioned transesterified algae oil and/or triglyceride oil.
  • Composition 1 was a clear liquid that did not exhibit any phase separation.
  • Composition A was unstable and separated into an clear, liquid upper phase and a brown jelly bottom phase.
  • Composition B was unstable as it showed sedimentation of a viscous lecithin-rich phase.
  • Composition C had to be stirred overnight in order to obtain a homogeneous viscous liquid.
  • Viscosities of the stable lipid compositions were measured with a capillary viscometer at room temperature. The results are summarised in Table 8.
  • Transesterified algae oil was prepared using an equimolar amount of ethanol:
  • the transesterified algae oil contained 6 wt.% monoglycerides and 2 wt.% diglycerides.
  • Lipid compositions were prepared by mixing 50 parts by weight of the de-oiled rapeseed lecithin of Example 1 with 50 parts by weight of the above mentioned transesterified algae oil.
  • the lipid composition so obtained was stable and had a viscosity of 140 mPa.s.
  • Transesterified algae oil was prepared using a sub-stochiometric amount of ethanol:
  • the mixture was first washed with 60 ml water and then with 60 ml citric acid (5 g/100 mL). During each washing step air was bubbled through the emulsion. After each washing the emulsion was kept at 50°C to promote phase separation. In each step the oil phase was removed by means of decanting.
  • the transesterified algae oil contained 19 wt.% monoglycerides and 2 wt.% diglycerides.
  • Lipid compositions were prepared by mixing 62 parts by weight of the de-oiled rapeseed lecithin of Example 1 with 38 parts by weight of the above mentioned transesterified algae oil.
  • the lipid composition so obtained was extremely stable and had a viscosity of 60 mPa.s.

Abstract

The invention relates to a pourable lipid composition comprising the following components: (a) 30-60 wt.% of lecithin component selected from glycerophospholipids, glycolipids and combinations thereof, including at least 20 wt.%, calculated by weight of the lipid composition, of glycerophospholipids; (b) 30-70 wt.% fatty acid ethyl esters; (c) 0.2-30 wt.% partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; (d) 0-30 wt.% triacylglycerides; wherein the lecithin component and the fatty acid ethyl esters are contained in the lipid composition in a weight ratio of less than 1.5:1; wherein the fatty acid ethyl esters comprise at least 35 wt.% of ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid, docosahexaenoic acid and combinations thereof; wherein the combination of components (a), (b), (c) and (d) comprises at least 90 wt.% of the composition; and wherein the combination of components (a) and (b) comprises at least 65 wt.% of the composition. The pourable lipid composition of the present invention is shelf-stable and provides very high levels of EPA and/or DHA in highly bioavailable form. The pourable lipid composition can suitably be manufactured using only lipids from plant sources.

Description

LIPID COMPOSITION COMPRISING OMEGA-3 FATTY ACIDS
TECHNICAL FIELD OF THE INVENTION
The invention relates to a pourable lipid composition comprising: a) lecithin component selected from glycerophospholipids, glycolipids and combinations thereof; b) fatty acid ethyl esters comprising ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid, docosahexaenoic acid and combinations thereof; c) partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; and d) optionally, triacylglycerides.
The invention also provides an oral dosage unit comprising the aforementioned lipid composition and a process for the manufacture of said lipid composition.
BACKGROUND OF THE INVENTION
Omega-3 fatty acids, also called w-3 fatty acids or n-3 fatty acids, are polyunsaturated fatty acids (PUFAs) characterized by the presence of a double bond three atoms away from the terminal methyl group in their chemical structure. The three main naturally occurring omega- 3 fatty acids are alpha-linolenic acid (ALA), eicosapentaenoic acid (EPA), and docosahexaenoic acid (DHA). ALA is found mainly in plant oils such as flaxseed, soybean, and canola oils. Sources of EPA and DHA include fish, fish oils, eggs from chickens fed EPA and DHA, squid oils, krill oil, and certain algae.
Humans, like all other mammals, are unable to synthesize the essential omega-3 fatty acid ALA and can only obtain it through diet. However, they can use ALA, when available, to form EPA and DHA, be it in only very small amounts. Therefore, getting EPA and DHA from foods or dietary supplements is the only practical way to increase levels of these omega-3 fatty acids in the human body. Because EPA is also a precursor to DHA, ensuring a sufficient level of EPA on a diet containing neither EPA nor DHA is harder both because of the extra metabolic work required to synthesize EPA and because of the use of EPA to metabolize into DHA. Medical conditions like diabetes or certain allergies may significantly limit the human body's capacity for metabolisation of EPA from ALA.
EPA acts as a precursor for prostaglandin-3 (which inhibits platelet aggregation), thromboxane-3, and leukotriene-5 eicosanoids. A recent multi-year study of Vascepa (ethyl eicosapentaenoic acid), a prescription drug containing only EPA, was shown to reduce heart attack, stroke, and cardiovascular death by 25% relative to a placebo in those with statin- resistant hypertriglyceridemia (Bhatt et al., Cardiovascular Risk Reduction with lcosapent Ethyl for Hypertriglyceridemia. New England Journal of Medicine (2019), 380: 11-22).
DHA is a major fatty acid in brain phospholipids and the retina. The potential roles of DHA in the mechanisms of Alzheimer's disease are under active research.
The European Food Safety Authority (EFSA) has approved health claims on omega-3 fatty acids. DHA/EPA for maintenance of normal cardiac function and normal (fasting) blood concentrations of triglycerides. DHA for maintenance of normal vision and normal brain function.
At the moment fish and krill are the major source of EPA and DHA used in supplements. The omega-3 oils from these sources, are deemed to be superior to omega-3 oils from plant sources, notably algae. Krill oil in particular is regarded as an excellent source of EPA and DHA. This is because krill oil, besides providing high levels of EPA and DHA, also provides the following favourable nutritional attributes:
• choline -an essential nutrient, and neurotransmitter precursor important to brain and muscle tissue;
• astaxanthin - a carotenoid with powerful antioxidant activity;
• phospholipids - EPA and DHA in krill oil are more efficiently absorbed by the human body as they are largely contained in phospholipids, whereas in other sources, such as fish oil, these omega-3 fatty acids are contained in triglycerides, which are insoluble and require bile salts for their emulsification and absorption via the lymphatic system.
Krill oil is an extract prepared from a species of Antarctic krill, Euphausia superba. Krill oil is characterized by a high glycerophospholipid content, phosphatidylcholine representing the bulk of the glycerophospholipids. Besides glycerophospholipids, krill oil contains triglycerides, diglycerides, monoglycerides and free fatty acids. Phospholipids typically represent 40-80 wt.% of the lipids contained in krill oil. Concentrations of the other lipids can vary considerably (see: Dan Xie et al., Antarctic Krill (Euphausia superba) Oil: A Comprehensive Review of Chemical Composition, Extraction Technologies, Health Benefits, and Current Applications ; Comprehensive Reviews in Food Science and Food Safety Vol.18 (2019), 514- 534). EPA and DHA typically represent 14.3-28.0 wt.% and 7.1-15.7 wt.%, respectively of the fatty acids present in krill oil.
Krill oils as well as fish oils have the drawback that there are concerns regarding sustainability. Furthermore, supplements based on these animal oil are not suited for vegetarians and vegans.
US 2017/0182074 describes a liquid composition having a viscosity of less than 3000 mPa.s when measured at a temperature within the range 25-70°C, wherein the composition comprises (i) at least 80% by weight of a phospholipid-containing krill extract which has a viscosity of at least 3000 mPa.s when measured at a temperature where the liquid composition has a viscosity of less than 3000 mPa-s and (ii) no more than 20% by weight of a viscosity-reducing agent. Suitable viscosity-reducing agents include lower alcohols, benzyl alcohol, glycerol, and glycols (e.g. propylene glycol, or a polyethylene glycol, vegetable oils, medium-chain triglycerides and polysorbates. The US patent application also describes an oral capsule for human use including an encapsulated liquid composition, wherein (a) the capsule is made from a material which includes glycerol, and (b) the liquid composition comprises purified krill phospholipids and glycerol.
CN 104306383 describes a soft capsule comprising phospholipid and unsaturated fatty acid ester. Example 1 describes the preparation of a capsule comprising a mixture of 65 parts by weight of phospholipid and 35 parts by weight of unsaturated fatty acid ester.
CN 108265090 describes a method or preparing an fat or oil composition containing almost the same phospholipid-type DHA and phospholipid-type EPA as natural Antarctic krill oil.
This fat or oil composition is prepared by transesterification of soybean lecithin with ethyl ester of EPA and ethyl ester of DHA.
US 2009/074857 describes lipid compositions comprising a mixture of serine glycerophospholipid conjugates with EPA and DHA.
Lipoid GmbH (“Water soluble composition containing omega-3-fatty acids for use in dietetics and food', Research Disclosure, Kenneth Mason Publications, Hampshire, UK, vol. 527, no. 13) relates to water soluble compositions comprising omega-3 fatty acids. WO 2013/072767 relates to compositions comprising:
• a fatty acid oil mixture comprising EPA and DHA, wherein the EPA and DHA are in a form chosen from free fatty acid, ethyl ester, triglyceride and phospholipid, and
• salicylate.
WO 2008/068276 relates to soft gelatin capsules containing a liquid or pasty lipophilic phase and aspirin.
WO 2015/142705 relates to dietary supplement compositions comprising an algae based oil having glycolipids and phospholipids and EPA fatty acids in combination with astaxanthin and hyaluronic acid or sodium hyaluronate.
SUMMARY OF THE INVENTION
The present invention relates to a pourable lipid composition that provides very high levels of EPA and/or DHA in highly bioavailable form and that provides a suitable alternative for krill oil. More particularly, the invention relates to a pourable lipid composition comprising the following components:
(a) 30-60 wt.% of lecithin component selected from glycerophospholipids, glycolipids and combinations thereof, including at least 20 wt.%, calculated by weight of the lipid composition, of glycerophospholipids;
(b) 30-70 wt.% fatty acid ethyl esters;
(c) 0.2-30 wt.% partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof;
(d) 0-30 wt.% triacylglycerides; wherein the lecithin component and the fatty acid ethyl esters are contained in the lipid composition in a weight ratio of less than 1.5:1; wherein the fatty acid ethyl esters comprise at least 35 wt.% of ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid, docosahexaenoic acid and combinations thereof; wherein the combination of components (a), (b), (c) and (d) comprises at least 90 wt.% of the composition; and wherein the combination of components (a) and (b) comprises at least 65 wt.% of the composition.
The pourable lipid composition of the present invention can suitably be manufactured using only lipids from plant sources, e.g. using omega-3 oil from algae and lecithin from soybean or rapeseed. The omega-3 oil can be converted into fatty acid ethyl esters by transesterification with ethanol.
Despite the high content of glycerophospholipids, the lipid composition of the present invention can be provided in a shelf-stable liquid form. Furthermore, the emulsifying action of the glycerophospholipids aids the absorption of the apolar fatty acid ethyl esters and thereby increases bioavailability of the omega-3 fatty acids.
The lipid composition of the present invention can contain high levels of EPA and/or DHA, allowing it to be used in supplements in the form of oral dosage units, such as capsules. Accordingly, the present invention also provides a dosage unit comprising 100-2000 mg of the aforementioned lipid composition.
Further provided is a process for the manufacture of the lipid composition of the present invention, said process comprising the steps: a) partially transesterifying algal oil with ethanol to produce a transesterified composition containing fatty acid ethyl ester and partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; b) combining the transesterified composition with lecithin.
This process offers the advantage that EPA and DHA containing ethyl esters and EPA and DHA containing partial glycerides are produced in one step.
Finally, the invention relates to the use of the present lipid composition in the treatment or prevention of cardiovascular-related disease, dry eye syndrome, Meibomian gland dysfunction, macular edema, Alzheimer’s disease and traumatic brain injury.
DETAILED DESCRIPTION OF THE INVENTION
A first aspect of the present invention relates to a pourable lipid composition comprising the following components:
(a) 30-60 wt.% of lecithin component selected from glycerophospholipids, glycolipids and combinations thereof, including at least 20 wt.%, calculated by weight of the lipid composition, of glycerophospholipids;
(b) 30-70 wt.% fatty acid ethyl esters; (c) 0.2-30 wt.% partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof;
(d) 0-30 wt.% triacylglycerides; wherein the lecithin component and the fatty acid ethyl esters are contained in the lipid composition in a weight ratio of less than 1.5:1, preferably in a weight ratio of less than 1.2:1, most preferably in a weight ratio of less than 1:1; wherein the fatty acid ethyl esters comprise at least 35 wt.% of ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid (EPA), docosahexaenoic acid (DHA) and combinations thereof; wherein the combination of components (a), (b), (c) and (d) comprises at least 90 wt.% of the composition; and wherein the combination of components (a) and (b) comprises at least 65 wt.%.
The term “pourable” as used herein means that at 20 °C the lipid composition can be poured out a container.
The “glycerides” as used herein refers to fatty acid esters of glycerol (triacylglycerides, diacylglycerides and monoacylglycerides).
The term “fatty acid” as used herein refers to a carboxylic acid with a long non-branched aliphatic chain of 6-24 carbon atoms.
The term “glycerophospholipids” as used herein refers to derivatives of glycerophosphoric acid that contains at least one fatty acid residue attached to the glycerol moiety. Examples of glycerophospholipids include phosphatidylcholine (PC), phosphatidylethanolamine (PE), phosphatidylinositol (PI), phosphatidylserine (PS) and phosphatidic acid (PA).
The term “glycolipid” as used herein refers a monosaccharide or oligosaccharide bound to a lipid moiety by means of a glycosidic bond.
Fatty acid concentrations as referred to herein, unless indicated otherwise, relate to the percentage by weight (% w/w) of the total combined amount of free fatty acids and fatty acid residues.
The combination of components (a)) and (b) preferably comprises at least 75wt.%, more preferably at least 85 wt.% and most preferably at least 90 wt.% of the present lipid composition. The combination of components (a), (b), (c) and (d) preferably comprises at least 92 wt.%, more preferably at least 93 wt.% and most preferably at least 94 wt.% of the lipid composition.
According to a particularly preferred embodiment of the present invention, all the components a) to d) of the lipid composition are plant derived. Most preferably, the entire lipid composition is plant derived.
The lipid composition of the present invention preferably provided at least 150 mg/g, more preferably 180-500 mg/g and most preferably 200-350 mg/g of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
In a further preferred embodiment, the lipid composition provides 12-80 mg/g, more preferably 18-70 mg/g and most preferably 24-65 mg/g alpha-linolenic acid (ALA).
The lipid composition of the present invention preferably comprises 33-58 wt.% lecithin component, more preferably 35-56 wt.% lecithin component, and most preferably 36-52 wt.% lecithin component.
The lipid composition of the present invention preferably comprises 25-50 wt.% glycerophospholipids, more preferably 27-45 wt.% glycerophospholipids, and most preferably 28-40 wt.% glycerophospholipids.
According to a particularly preferred embodiment, the lecithin component is obtained from soybean and/or rapeseed as the glycerophospholipids of these plant sources contain significant levels of omega-3 fatty acid residues in the form of alpha-linolenic acid.
Preferably 2-15 wt.%, more preferably 3-12 wt.% and most preferably 4-9 wt.% of the fatty acid residues in the glycerophospholipids is alpha-linolenic acid residue (ALA).
Unlike the fatty acid ethyl esters, the glycerophospholipids of the present invention typically do not contain more than a limited amount of EPA and/or DHA. Accordingly, in a preferred embodiment, 0-10 wt.%, more preferably 0-5 wt.% and most preferably 0-3 wt.% of the fatty acid residues in the glycerophospholipids are omega-3 fatty acids selected from EPA, DHA and combinations thereof. Unsaturated fatty acid residues preferably constitute at least 75 wt.%, more preferably at least 80 wt.% and most preferably at least 85 wt.% of the fatty acid residues in the glycerophospholipids.
Polyunsaturated fatty acid residues preferably constitute at least 25 wt.%, more preferably at least 28 wt.% and most preferably at least 30 wt.% of the fatty acid residues in the glycerophospholipids.
The glycerophospholipids in the lipid composition preferably comprise at least 10 wt.% phosphatidylcholine, more preferably 20-80 wt.% phosphatidylcholine, most preferably 30-60 wt.% phosphatidylcholine.
The glycerophospholipids in the lipid composition preferably comprise at least 5 wt.% phosphatidylethanolamine, more preferably 10-50 wt.% phosphatidylethanolamine, most preferably 20-35 wt.% phosphatidylethanolamine.
The lipid composition preferably comprises 35-66 wt.% fatty acid ethyl esters, more preferably 38-64 wt.% fatty acid ethyl esters and most preferably 40-63 wt.% fatty acid ethyl esters.
According to another preferred embodiment, the fatty acid ethyl esters comprise 0.5-30 wt.% eicosapentaenoic acid ethyl esters, more preferably 3-20 wt.% eicosapentaenoic acid ethyl esters, most preferably 5-15 wt.% eicosapentaenoic acid ethyl esters.
According to a preferred embodiment, the fatty acid ethyl esters comprise 30-60 wt.% docosahexaenoic acid ethyl esters, more preferably 32-50 wt.% docosahexaenoic acid ethyl esters, most preferably 35-40 wt.% docosahexaenoic acid ethyl esters.
Preferably, eicosapentaenoic acid ethyl esters and docosahexaenoic acid ethyl esters together constitute at least 30 wt.% , more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid ethyl esters in the lipid composition.
The lipid composition preferably comprises partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof. Partial glycerides containing omega-3 fatty acids may be produced in the preparation of the ethyl esters of fatty acids by transesterification of triglycerides with ethanol or they can be produced separately by transesterification of omega-3 oil with glycerol. The lipid composition preferably comprises 0.2-10 wt.%, more preferably 0.3-6 wt.% and most preferably 0.4-4 wt.% of the partial glycerides.
According to a particularly preferred embodiment at least 30 wt.%, more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid residues in the partial glycerides are residues of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
Triacylglycerides are preferably comprised in the lipid composition in a concentration of 0.1- 20 wt.%, more preferably a concentration of 0.2-10 wt.% and most preferably in a concentration of 0.3-5 wt.%.
Preferably, at least 35 wt.%, more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid residues in the triacylglycerides are residues of omega-3 fatty acids selected from EPA, DHA and combinations thereof
The ratio on a weight basis of the glycerophospholipids to the fatty acid ethyl esters in the lipid composition is preferably in the range of 1:3 to 1:1, more preferably in the range of 1:2.8 to 1:1.1, and most preferably in the range of 1:2.5 to 1:1.2.
The ratio on a weight basis of the partial glycerides to the triacylglycerides in the lipid composition is preferably at least 1:30, more preferably at least 1:20, and most preferably in the range of 1:15 to 3:1.
In an advantageous embodiment, the lipid composition further comprises 0.001-1.5 wt.%, more preferably 0.1-1.2 wt.% and most preferably 0.3-0.9 wt.% carotenoids selected from beta carotene, lutein, astaxanthin, zeaxanthine.
According to a particularly preferred embodiment, the lipid composition comprises 1-2,000 ppm (mg/kg), more preferably 100-1,500 ppm, most preferably 300-900 ppm astaxanthin.
In another preferred embodiment, the lipid composition further comprises 0.01-2 wt.%, more preferably 0.1 -1.5 wt.% and most preferably 0.3-1 wt.% tocopherol.
The pourable lipid composition of the present invention preferably has a viscosity of not more than 10,000 cP, more preferably of 200 to 9000 cP at 20 °C and a shear rate of 100 s 1. The pourable lipid composition preferably shows less than 5 wt.%, more preferably less than 2 wt.% and most preferably less than 1 wt.% phase separation when the composition is kept in a sealed glass container at 20°C for 2 months. The wt.% phase separation is determined gravimetrically after decantation.
Another aspect of the invention relates to an oral dosage unit comprising 100-2000 mg, more preferably comprising 300-1500 mg, most preferably comprising 400-1000 mg of the pourable lipid composition of the invention.
Preferably, the oral dosage unit provides 150-500 mg, more preferably 200-400 mg and most preferably 250-350 mg of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
In a further preferred embodiment, the oral dosage unit provides 10-100 mg, more preferably 15-80 mg and most preferably 20-50 mg ALA.
The oral dosage unit of the present invention preferably is a capsule that is filled with the pourable lipid composition. Preferably, the capsule comprises a gel film, more preferably a vegetarian gel film, i.e. a gel film that does not contain animal products such as gelatin.
The capsule comprising the gel film preferably has a water content in the range of 5 to 30 wt.%, more preferably of 8 to 25 wt.%, most preferably in the range of 10 to 22 wt.%.
The inventors have observed that water present in the capsule tends to migrate from the capsule towards the lipid composition, possibly due to the high phospholipid content of the lipid composition. This migration of water has an adverse effect on the capsule in that the corresponding lowering of the water content causes the gel film to become less elastic, brittle and fragile. At the same time, the increase in water content of the lipid composition can cause phase separation in the lipid composition, especially near the interface with the capsule.
The inventors have found that this unwanted water migration can be prevented or at least minimised by including a polar liquid in the lipid composition. Examples of polar liquids that may be employed include water, ethyl lactate, glycerol, ethylene glycol, propylene glycol, polyethylene glycol and combinations thereof. More preferably, the polar liquid is selected from water, ethyl lactate and combinations thereof. Most preferably, the polar liquid is ethyl lactate. The aforementioned polar liquid is preferably comprised in the pourable lipid composition in a concentration of 0.5-10 wt.%, more preferably in a concentration of 1-8 wt.% and most preferably in a concentration of 1.5-6 wt.%.
Yet another aspect of the invention relates to a process for the manufacture of a lipid composition as described herein before, said process comprising the steps: a) partially transesterifying algal oil with ethanol to produce a transesterified composition containing fatty acid ethyl ester and partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; b) combining the transesterified composition with lecithin.
In a preferred embodiment, the present process yields a pourable lipid composition as defined herein before.
The transesterified composition that is produced by the partial transesterification of algal oil preferably comprises 0.4-20 wt.%, more preferably 0.6-12 wt.% and most preferably 0.8-8 wt.% of the partial glycerides.
Preferably, at least 30 wt.%, more preferably at least 40 wt.% and most preferably at least 50 wt.% of the fatty acid residues in the algal are residues of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
The algal oil used as a staring material in the present process preferably comprises at least 25 wt.%, more preferably at least 50 wt.% and most preferably at least 80 wt.% triacylglycerides.
The algal oil employed in the present process preferably is an oil extracted from one or more of the genera Schizochytrium, Isochrysis, Nannochloris, Tetracelmis, Nannochloropsis, Chlorella. Most preferably, the algal oil is extracted from Schizochytrium.
In one embodiment of the present process, the transesterification is catalysed by an ethoxide salt selected from lithium ethoxide, sodium ethoxide, potassium ethoxide, preferably the ethoxide salt is sodium ethoxide.
In another embodiment of the present process, the transesterification is catalysed by a lipase. The lecithin used in the present process is preferably selected from rapeseed lecithin, soy lecithin, sunflower lecithin, corn lecithin, cottonseed lecithin, sesame lecithin, perilla lecithin, linseed lecithin and combinations thereof. More preferably, the lecithin is selected from rapeseed lecithin, soy lecithin and combinations thereof.
The lecithin employed in the present process preferably has a glycerophospholipid content of at least 40 wt.%, more preferably of at least 55 wt.% and most preferably of 60-95 wt.%.
In the present process, prior to transesterification the ethanol and the algal oil are preferably combined in a weight ratio of 1:2 to 1:20, more preferably in a weight ratio of 1:2.5 to 1:16 and most preferably in a weight ratio of 1 :3 to 1 :6.
Any ethanol remaining in the transesterified composition is preferably removed before the composition is combined with the lecithin.
The transesterified composition and the lecithin are preferably combined in a weight ratio of 40:60 to 70:30, more preferably in a weight ratio of 42:58 to 68:32 and most preferably in a weight ratio of 45:55 to 65:35.
Yet another aspect of the present invention relates to the use of the lipid composition of the present invention or of the oral dosage unit of the present invention for use in the treatment or prevention of cardiovascular-related disease, dry eye syndrome, Meibomian gland dysfunction, macular edema Alzheimer’s disease and traumatic brain injury. Most preferably, the lipid composition or oral dosage unit is used in the treatment or prevention of cardiovascular-related disease, more particularly a cardiovascular-related disease selected from high blood pressure, coronary heart disease, dyslipidemia, congestive heart failure and stroke.
Preferably, said use comprises orally administering of the lipid composition or the oral dosage unit. More preferably, the use comprises oral administration to provide a dose of at least 500 mg, more preferably a dose of 600-2,000 mg and most preferably a dose of 750- 950 mg of omega-3 fatty acids selected from EPA, DHA and combinations thereof.
The invention is further illustrated by the following non-limiting examples. EXAMPLES
Example 1
Transesterified algae oil was prepared as follows. 100.3 g of omega-3 triglyceride oil from Schizochytrium sp. (DSM life’s Omega 60, 15% EPA 30% DHA) were warmed up to 50°C in a water bath under stirring and under nitrogen. 0.50 g of NaOH and 199.3 g of anhydrous ethanol were mixed at ambient temperature until complete dissolution. The ethanolic NaOH solution was added to the triglyceride oil. The mixture was initially cloudy but cleared after 1 min. The reaction was stopped after 5 min. The transesterified oil was mixed with 400 ml of hot tap water in a 1L-separating funnel which led to a stable, milky mixture. Sodium chloride was added to speed up phase separation. After two hours, both phases were still cloudy. The upper phase was washed a second time with 300 ml of demineralized water. The washed transesterified oil was filtered on a pleated filter to reduce its residual water amount.
Powdered de-oiled rapeseed lecithin (98.5% acetone insolubles) was partially extracted with ethanol - water to obtain an extract rich in PC and PE and leaving a residue containing other complex and neutral lipids according to a method described by Patil et al. ( Extraction and purification of phosphatidylcholine from soyabean lecithin, Separation and Purification Technology 75 (2010) 138-144).
48.8 g of transesterified oil were mixed with 29.8 g of refined lecithin in a beaker at 50° under stirring during 15 min.
The lipid composition so obtained had a very low, water-like viscosity and was stable under different storage conditions (room temperature, 4 °C in refrigerator) for days. The composition of the lipid composition is shown in Table 1.
Table 1
Figure imgf000014_0001
1 16% phosphatidylcholine, 4% phosphatidyl ethanolamine, 10% phosphatidylinositol (De oiled rapeseed lecithin powder, Lecico RAP P 200 IP) Example 2
Transesterified algae oil was prepared as follows. 570.3 g of omega-3 triglyceride oil from Schizochytrium sp. (DSM life’s Omega 60, 15% EPA 30% DHA) were warmed up to 50°C in a 1 L stirred reactor on a water bath under nitrogen. 2.0 g of NaOH and 199.9 g of anhydrous ethanol were mixed at ambient temperature until complete dissolution. The NaOH ethanolic solution was added to the triglyceride oil. After 2 hours 300 g deionised water were added to stop the reaction and to wash out salts and other byproducts. The mixture was left to settle for 1 hour and 20 minutes and the water phase was withdrawn. The procedure was repeated with another 200 ml of deionised water and the water phase was again withdrawn after a settling time of 2 hours.
The transesterified oil phase so obtained was mixed with 5 g micro-crystalline cellulose to bind residual water. After letting the cellulose settle overnight the oil was filtered over paper filter to yield 511.15g of transesterified algae oil.
510.0 g of the transesterified oil were mixed with 510.1 g de-oiled rapeseed lecithin (98.5% acetone insolubles) by repeatedly blending with a kitchen blender until no particles of lecithin were visible any more. Finally 10 g of astaxanthin oleoresin (10% astaxanthin) were admixed by the same mixing device.
The pourable lipid composition so obtained stayed homogeneous during several days at room temperature as well as at 4 °C in a refrigerator.
The composition of the lipid composition is shown in Table 2.
Table 2
Figure imgf000015_0001
1 14% phosphatidylcholine, 8.4% phosphatidyl ethanolamine, 8.9% phosphatidylinositol, 2.0% phosphatidic acid, and 2.0% of lyso-phosphatidylcholine
Example 3
Transesterified algae oil was prepared as follows. 10.04 kg of omega-3 triglyceride oil from Schizochytrium sp. (DSM life’s Omega 60, 15% EPA 30% DHA) were warmed up to 50°C in a 20 L stirred reactor with a heating jacket and recirculated water heater under nitrogen. 35.0 g of NaOH and 3.45 kg of anhydrous ethanol were mixed at ambient temperature until complete dissolution. After equilibrating the triglyceride oil at 50°C, the NaOH ethanolic solution was added to the oil by a dosage pump. After 2 hours of reaction 5 L deionised water were added to stop the reaction and to wash out salts and other byproducts. The mixture was left to settle for 2 hours before the water phase was withdrawn. The procedure was repeated with another 3.5 L of deionised water and the water phase was again withdrawn after a settling time of 10 minutes. 400 g microcrystalline cellulose were added to the transesterified oil to bind residual water. After letting the cellulose settle over night the oil was transferred from the reactor to a storage tank via a 1 micrometer in-line filter.
18.99 kg of the transesterified algae oil were mixed with 18.95 kg de-oiled rapeseed lecithin (98.5% acetone insolubles) in a 80 L mixing vessel equipped with a high-shear mixer. While lecithine was added the mixer was operated at maximum speed. Afterwards it was left on for 2 hours at medium speed until there were no visible particles of lecithin any more. Then 340 g of astaxanthin oleoresin (10% astaxanthin) and 425 g of a tocopherol mixture were added while blending at high speed for 15 minutes.
The pourable lipid composition so obtained was filled into bottles and used for test runs for encapsulation into softgel capsules. The composition of the lipid composition is shown in Table 3.
Table 3
Figure imgf000016_0001
The composition and characteristics of the pourable lipid composition are shown in Table 4. Table 4
Figure imgf000017_0001
Example 4
Vegetarian Softgel capsules were prepared containing 850 mg of the pourable composition of Example 3, using Vegesoft® capsules, supplied by Eurocaps, Tredegar, South Wales, NP224EF, United Kingdom..
After one month storage under ambient conditions, the filled capsules still exhibited adequate mechanical integrity.
Example 5
Experiments were carried out to establish the impact of different pourable lipid compositions on the capsule material of the capsules described in Example 4. The compositions of the different pourable lipid compositions are shown in Table 5 (lipid composition 1 is identical to the lipid composition of Example 2).
Table 5
Figure imgf000017_0002
Pieces of Vegesoft® capsules (0.16 gram) were submerged in 15 grams of pourable lipid composition and left in there for three days. At the end of the storage time the pieces were removed from the lipid compositions, washed with hexane and allowed to dry. The weight of the pieces that had been stored in the different lipid compositions was compared with that of the original pieces. Also changes in the physical characteristics of the capsule materials and the lipid compositions were determined. The results are shown in Table 6.
Table 6
Figure imgf000018_0001
The observed weight loss is believed to have been caused by migration of water of from the capsule material into the lipid composition, possibly triggered by the high phospholipid content of the lipid composition. Removal of water from the capsule material reduces the elasticity and renders the material more fragile. Migration of water into the pourable liquid compositions can cause destabilisation resulting in the formation of a viscous layer on the surface of the capsule material.
Example 6
Transesterified algae oil was prepared using a two-fold excess of ethanol:
• 175 g of non winterized algae oil having a DHA content of 45.8% and an EPA content of 1.5% (AlgalPure DHA®, ex Bioriginal) were esterified with 54.6 g ethanol (PhEUR >99,5%), using 4.8 g sodium ethanolate as catalyst. The reaction mixture was stirred on a water bath at 50 °C for 1 h.
• Next, the mixture was washed twice with 80 ml water and once with 80 ml citric acid (5 g/100 ml_). During each washing step air was bubbled through the emulsion. After each washing the emulsion was kept at 50°C to promote phase separation. In each step the oil phase was removed by means of decanting.
• Finally, the decanted oil was filtered over cellulose to remove moisture.
The transesterified algae oil contained 4 wt.% partial glycerides in the form of monoglycerides.
Lipid compositions were prepared by mixing the de-oiled rapeseed lecithin of Example 1 with the above mentioned transesterified algae oil and/or triglyceride oil.
The compositions of the lipid compositions so obtained are shown in Table 7. Table 7
Figure imgf000019_0001
1 Added in the form of mono/diglycerides (SaporePuro, Gioia Group S.R.L., Italy)
2 DSM life’s Omega 60, 15% EPA 30% DHA
Composition 1 was a clear liquid that did not exhibit any phase separation.
Composition A was unstable and separated into an clear, liquid upper phase and a brown jelly bottom phase.
Composition B was unstable as it showed sedimentation of a viscous lecithin-rich phase.
Composition C had to be stirred overnight in order to obtain a homogeneous viscous liquid.
Viscosities of the stable lipid compositions were measured with a capillary viscometer at room temperature. The results are summarised in Table 8.
Table 8
Figure imgf000019_0002
Example 7
Transesterified algae oil was prepared using an equimolar amount of ethanol:
• 192 g of algae oil containing 15% EPA and 30% DHA (DSM life’s Omega 60) were esterified with 26 g ethanol (PhEUR >99,5%), using 5.7 g sodium ethanolate as catalyst. The reaction mixture was stirred on a water bath at 50 °C for 1 h.
• Next, the mixture was successively washed with 60 ml water and with 60 ml citric acid (5 g/100 ml_). During each washing step air was bubbled through the emulsion. After each washing the emulsion was kept at 50°C to promote phase separation. In each step the oil phase was removed by means of decanting.
• Finally, the decanted oil was filtered over cellulose to remove moisture.
The transesterified algae oil contained 6 wt.% monoglycerides and 2 wt.% diglycerides. Lipid compositions were prepared by mixing 50 parts by weight of the de-oiled rapeseed lecithin of Example 1 with 50 parts by weight of the above mentioned transesterified algae oil.
The lipid composition so obtained was stable and had a viscosity of 140 mPa.s.
Example 8
Transesterified algae oil was prepared using a sub-stochiometric amount of ethanol:
• 191 g of algae oil containing 15% EPA and 30% DHA (DSM life’s Omega 60) were esterified with 15 g ethanol (PhEUR >99,5%), using 5.1 g sodium ethanolate as catalyst. The reaction mixture was stirred on a water bath at 50 °C for 1 h.
• The mixture was first washed with 60 ml water and then with 60 ml citric acid (5 g/100 mL). During each washing step air was bubbled through the emulsion. After each washing the emulsion was kept at 50°C to promote phase separation. In each step the oil phase was removed by means of decanting.
• Finally, the decanted oil was filtered over cellulose to remove moisture.
The transesterified algae oil contained 19 wt.% monoglycerides and 2 wt.% diglycerides.
Lipid compositions were prepared by mixing 62 parts by weight of the de-oiled rapeseed lecithin of Example 1 with 38 parts by weight of the above mentioned transesterified algae oil.
The lipid composition so obtained was extremely stable and had a viscosity of 60 mPa.s.

Claims

1. A pourable lipid composition comprising the following components:
(a) 30-60 wt.% of lecithin component selected from glycerophospholipids, glycolipids and combinations thereof, including at least 20 wt.%, calculated by weight of the lipid composition, of glycerophospholipids;
(b) 30-70 wt.% fatty acid ethyl esters;
(c) 0.2-30 wt.% partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof;
(d) 0-30 wt.% triacylglycerides; wherein the lecithin component and the fatty acid ethyl esters are contained in the lipid composition in a weight ratio of less than 1.5:1; wherein the fatty acid ethyl esters comprise at least 35 wt.% of ethyl esters of omega-3 fatty acids selected from eicosapentaenoic acid, docosahexaenoic acid and combinations thereof; wherein the combination of components (a), (b), (c) and (d) comprises at least 90 wt.% of the composition; and wherein the combination of components (a) and (b) comprises at least 65 wt.% of the composition.
2. The lipid composition according to claim 1, wherein the combination of components (a) and (b) comprises at least 75 wt.% of the composition.
3. The lipid composition according to claim 1 or 2, wherein the composition comprises 25- 50 wt.% glycerophospholipids,.
4. The lipid composition according to any one of the preceding claims, wherein 2-10 wt.% of the fatty acid residues in the glycerophospholipids is alpha-linolenic acid residue.
5. The lipid composition according to any one of the preceding claims, wherein the fatty acid ethyl esters comprise 0.5-30 wt.% eicosapentaenoic acid ethyl esters.
6. The lipid composition according to any one of the preceding claims, wherein the fatty acid ethyl esters comprise 30-60 wt.% docosahexaenoic acid ethyl esters.
7. The lipid composition according to any one of the preceding claims, wherein the composition comprises 35-66 wt.% fatty acid ethyl esters.
8. The lipid composition according to any one of the preceding claims, wherein the composition comprises 0.2-10 wt.% of the partial glycerides.
9. The lipid composition according to any of the preceding claims, wherein the ratio on a weight basis of the glycerophospholipids to the fatty acid ethyl esters is 1:3 to 1:1.
10. The lipid composition according to any of the preceding claims, wherein the glycerophospholipids comprise at least 10 wt.% phosphatidylcholine, preferably 20- 80wt.% phosphatidylcholine, most preferably 30-60 wt.% phosphatidylcholine.
11. An oral dosage unit comprising 100-2,000 mg of the lipid composition according to any of the preceding claims, preferably comprising 300-1 ,500 mg of the lipid composition, most preferably 400-1 ,000 mg of the lipid composition.
12. Oral dosage unit according to claim 11 , wherein the oral dosage unit comprises a capsule that comprises a gel film having a water content in the range of 5 to 30 wt.%, and wherein the capsule holds the lipid composition, said lipid composition containing 0.5-10 wt.% of polar liquid selected from water, ethyl lactate, glycerol, ethylene glycol, propylene glycol, polyethylene glycol and combinations thereof.
13. A process for the manufacture of a lipid composition according to any of the preceding claims, comprising the steps: a) partially transesterifying algal oil with ethanol to produce a transesterified composition containing fatty acid ethyl ester and partial glycerides selected from monoacylglycerides, diacylglycerides and combinations thereof; b) combining the transesterified composition with lecithin.
14. The process according to claim 13, wherein the algal oil is an oil extracted from one or more of the genera Schizochytrium, Isochrysis, Nannochloris, Tetracelmis, Nannochloropsis, Chlorella.
15. Lipid composition according to any one of claims 1-11 or oral dosage unit according to claim 12 for use in the treatment or prevention of cardiovascular-related disease, dry eye syndrome, Meibomian gland dysfunction, macular edema Alzheimer’s disease and traumatic brain injury.
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