`Tilseth et al.
`
`(10) Patent No.:
`(45) Date of Patent:
`
`US 8,372,812 B2
`Feb. 12, 2013
`
`US008372812B2
`
`(54) PHOSPHOLIPID AND PROTEIN TABLETS
`(75) Inventors: Snorre Tilseth, Bergen (NO); Nils
`Hoem, Oslo (NO)
`(73) Assignee: Aker Biomarine ASA, Oslo (NO)
`(*) Notice:
`Subject to any disclaimer, the term of this
`patent is extended or adjusted under 35
`U.S.C. 154(b) by 362 days.
`(21) Appl. No.: 12/711,822
`
`(22) Filed:
`
`Feb. 24, 2010
`
`(65)
`
`Prior Publication Data
`US 2010/0227792 A1
`Sep. 9, 2010
`
`Related U.S. Application Data
`(60) Provisional application No. 61/155,758, filed on Feb.
`26, 2009.
`
`(51) Int. Cl.
`(2006.01)
`A6 IK38/17
`(2006.01)
`A6 IK3I/01
`(2006.01)
`A6 IK9/20
`(2006.01)
`46K9/38
`(2006.01)
`A6 IK9/42
`(52) U.S. Cl. ..................... 514/21.92: 514/762; 424/464;
`424/476; 424/477
`(58) Field of Classification Search ........................ None
`See application file for complete search history.
`
`(56)
`
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`Primary Examiner — Christina Bradley
`(74) Attorney, Agent, or Firm — Casimir Jones SC
`(57)
`ABSTRACT
`A new method for krill meal production has been developed
`using a two step cooking process. In the first step the proteins
`and phospholipids are removed from the krill and precipitated
`as a coagulum. In the second stage the krill without phospho
`lipids are cooked. Following this, residual fat and astaxanthin
`are removed from the krill using mechanical separation meth
`ods. A novel krill meal product with superior nutritional and
`technical properties is prepared.
`16 Claims, 7 Drawing Sheets
`RIMFROST EXHIBIT 1140 Page 0001
`
`
`
`US 8,372,812 B2
`Page 2
`
`WO
`WO
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`* cited by examiner
`
`RIMFROST EXHIBIT 1140 Page 0003
`
`
`
`U.S. Patent
`
`Feb. 12, 2013
`
`Sheet 1 of 7
`
`US 8,372,812 B2
`
`FIGURE 1
`
`KRELL WATER
`
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`
`
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`
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`
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`
`RIMFROST EXHIBIT 1140 Page 0004
`
`
`
`U.S. Patent
`
`Feb. 12, 2013
`
`Sheet 2 of 7
`
`US 8,372,812 B2
`
`
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`RIMFROST EXHIBIT 1140 Page 0005
`
`
`
`U.S. Patent
`
`Feb. 12, 2013
`
`Sheet 3 of 7
`
`US 8,372,812 B2
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`RIMFROST EXHIBIT 1140 Page 0006
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`U.S. Patent
`
`Feb. 12, 2013
`
`Sheet 4 of 7
`
`US 8,372,812 B2
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`FIGURE 4
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`Sheet 6 of 7
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`
`
`
`1.
`PHOSPHOLIPID AND PROTEIN TABLETS
`
`CROSS REFERENCE TO RELATED
`APPLICATIONS
`
`This application claims priority to U.S. Provisional Appli
`cation Ser. No. 61/155,758, filed: Feb.26, 2009, which is here
`incorporated by reference in its entirety.
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`FIELD OF THE INVENTION
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`The invention relates to tablets comprising phospholipids
`and protein, and in particular to the production of tablets
`containing astaxanthin and phospholipids comprising
`omega-3 fatty acid moieties.
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`BACKGROUND OF THE INVENTION
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`Krill is a small crustacean which lives in all the major
`oceans world-wide. For example, it can be found in the Pacific
`Ocean (Euphausia pacifica), in the Northern Atlantic (Mega
`nyctiphanes norvegica) and in the Southern Ocean off the
`coast of Antarctica (Euphausia superba). Krill is a key spe
`cies in the oceanas it is the food source for many animals such
`as fish, birds, sharks and whales. Krill can be found in large
`quantities in the ocean and the total biomass of Antarctic krill
`(E. superba) is estimated to be in the range of 300-500 million
`metric tons. Antarctic krill feeds on phytoplankton during the
`short Antarctic Summer During winter, however, its food Sup
`ply is limited to ice algae, bacteria, marine detritus as well as
`depleting body protein for energy. Virtue et al., Mar. Biol.
`126,521-527. For this reason, the nutritional values of krill
`vary during the season and to Some extent annually. Phlegeret
`al., Comp. Biochem. Physiol. 131B (2002) 733. In order to
`accommodate variations in food Supply, krill has developed
`an efficient enzymatic digestive apparatus resulting in a rapid
`breakdown of the proteins into amino acids. Ellingsen et al.,
`Biochem. J. (1987) 246, 295-305. This autoproteolysis is
`highly efficient also post mortem, making it a challenge to
`catch and store the krill in a way that preserves the nutritional
`quality of the krill. Therefore, in order to prevent the degra
`dation of krill the enzymatic activity is either reduced by
`storing the krill at low temperatures or the krill is made into a
`krill meal.
`During the krill meal process the krill is cooked so that all
`the active enzymes are denatured in order to eliminate all
`enzymatic activity. Krill is rich in phospholipids which act as
`emulsifiers. Thus it is more difficult to separate water, fat and
`proteins using mechanical separation methods than it is in a
`regular fish meal production line. In addition, krill becomes
`Solid, gains weight and loose liquid more easily when mixed
`with hot water. Eventually this may lead to a gradual buildup
`of coagulated krill proteins in the cooker and a non-continu
`ous operation due to severe clogging problems. In order to
`alleviate this, hot steam must be added directly into the
`cooker. This operation is energy demanding and may also
`result in a degradation of unstable bioactive components in
`the krill Such as omega-3 fatty acids, phospholipids and astax
`anthin. The presence of these compounds, make krill oil an
`attractive source as a food Supplement, a functional food
`products and a pharmaceutical for the animal and human
`applications.
`Omega-3 fatty acids have recently been shown to have
`potential effect of preventing cardiovascular disease, cogni
`tive disorders, joint disease and inflammation related diseases
`Such as rheumatoid arthritis. Astaxanthin is a strong antioxi
`dant and may therefore assist in promoting optimal health.
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`US 8,372,812 B2
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`Hence, there is a need for a method of processing krill into a
`krill meal at more gentle conditions which prevents the deg
`radation of these valuable bioactive compounds.
`
`SUMMARY OF THE INVENTION
`
`The invention relates to processing crustaceans such as
`krill to provide oil and meal products, and in particular to the
`production of oils and other lipid extracts containing astax
`anthin and phospholipids comprising omega-3 fatty acid moi
`eties and meal rich in astaxanthin.
`In some embodiments, the present invention provides com
`positions comprising less than about 150, 100, 10, 5, 2 or 1
`mg/kgastaxanthin or from about 0.1 to about 1, 2, 5, 10 or 200
`mg/kg astaxanthin, preferably endogenous, naturally occur
`ring astaxanthin, also in the form of astaxanthin esters, from
`about 20% to about 50%, 15% to 45%, or 25% to 35%
`phospholipids on a w/w basis, and about 15% to 60%, about
`20% to 50%, or about 25% to 40% protein on a w/w basis,
`wherein said phospholipids comprise omega-3 fatty acid resi
`dues. In some embodiments, the composition comprises a
`lipid fraction having an omega-3 fatty acid content of from
`about 5% to about 30%, from 10% to about 30%, or from
`about 12% to about 18% on a w/w basis. In some embodi
`ments, the phospholipids comprise greater than about 60%,
`65%, 80%, 85% or 90% phosphatidylcholine on a w/w basis.
`In some embodiments, the phospholipids comprise less than
`about 15%, 10%, 8% or 5% ethanolamine on a w/w basis. In
`Some embodiments, the compositions comprise from about
`1% to 10%, preferably 2% to 8%, and most preferably about
`2% to 6% alkylacylphosphatidylcholine. In some embodi
`ments, the compositions comprise from about 30% to about
`70% triacylglycerol on a w/w basis. In further embodiments,
`the compositions comprise less than about 1% cholesterol. In
`some embodiments, the protein comprises from about 8% to
`about 14% leucine on awfw basis and from about 5% to 11%
`isoleucine on a W/w basis.
`In some embodiments, the present invention comprises an
`aqueous phase and a Solid phase, said solid phase comprising
`from about 20% to about 50% phospholipids on a w/w basis,
`and about 20% to 50% protein on a w/w basis, wherein said
`phospholipids comprise from about 10% to about 20%
`omega-3 fatty acid residues.
`In other embodiments, the present invention provides krill
`compositions comprising astaxanthin, a protein fraction, and
`a lipid fraction, wherein said lipid fraction comprises less
`than about 10%, 5% or 3% phospholipids on a w/w basis. In
`Some embodiments, the phospholipids comprise less than
`about 15%, 10% or 5% phosphatidylcholine on a w/w basis.
`In some embodiments, the present invention provides a
`krill meal comprising astaxanthin and from about 8% to about
`31% lipids, preferably from about 8% to about 10 or 18%
`lipids, wherein said lipids comprises greater than about 80%
`neutral lipids on a w/w basis. In some embodiments, the krill
`meal comprises less than about 15%, 10%, 5%, 3% or 1%
`phospholipids. In some embodiments, the phospholipids
`comprise less than about 15%, 10% or 5% phosphatidylcho
`line on a w/w basis.
`In some embodiments, the present invention provides
`methods of preparing a phospholipid composition from bio
`logical material or biomass comprising: mixing said biologi
`cal material or biomass with waterata suitable temperature to
`form a solid phase and an aqueous phase comprising phos
`pholipids and proteins; separating said solid phase from said
`aqueous phase; heating said aqueous phase at a temperature
`Sufficient to form a phospholipid-protein precipitate; and
`separating said phospholipid-protein precipitate from said
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`US 8,372,812 B2
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`aqueous phase. In some embodiments, the present invention
`provides a phospholipid-protein precipitate obtained by using
`the foregoing method. In some embodiments, the biological
`material or biomass is krill. In other embodiments, the bio
`logical material or biomass is selected from crabs, shrimp,
`calanus, plankton, crayfish, eggs or other phospholipid con
`taining biological materials or biomass. In some embodi
`ments, the methods further comprise the step of forming a
`meal from said Solid phase. In some embodiments, the step of
`forming a meal comprises: heating the Solid phase in the
`presence of water, separating fat and protein in said Solid
`phase; and drying said protein to form a meal. In some
`embodiments, the processes further comprise the steps of
`pressing and drying the coagulum to form a coagulum meal.
`In some embodiments, the drying is by hot air or steam. In
`Some embodiments, the present invention provides a phos
`pholipid-protein precipitate obtained by using the foregoing
`method. In some embodiments, the present invention pro
`vides a composition comprising a krill Solid phase according
`to the foregoing methods. In some embodiments, the present
`invention provides a krill meal obtained by the foregoing
`methods.
`In some embodiments, the present invention provides pro
`cesses comprising: extracting a first lipid fraction from a krill
`biomass; extracting a second lipid fraction from a krill bio
`mass; and blending said first lipid fraction and said second
`lipid fraction to provide a krill lipid composition having a
`desired composition. In some embodiments, the one or more
`of the extracting steps are performed in the absence of Sub
`stantial amounts of organic Solvents. In some embodiments,
`the first lipid fraction is extracted by: mixing krill with water
`at a suitable temperature to form a solid phase and an aqueous
`phase comprising phospholipids and protein; separating said
`Solid phase from said aqueous phase; heating said aqueous
`phase at a temperature Sufficient to form a phospholipid
`protein precipitate; separating said phospholipid-protein pre
`cipitate from said aqueous phase; and separating said phos
`pholipids from said protein. In some embodiments, the
`second lipid fraction is extracted by: heating the Solid phase in
`the presence of water; and separating fat and protein in said
`solid phase. In some embodiments, the first lipid fraction
`comprises a phospholipid fraction comprising greater than
`about 90% phosphatidylcholine on a w/w basis. In some
`embodiments, the second lipid fraction comprises greater
`than about 80% neutral lipids on a w/w basis.
`In some embodiments, the present invention provides pro
`cesses of producing a phospholipid composition from bio
`logical material or biomass comprising: mixing said biologi
`cal material or biomass with water to increase the temperature
`of said biological material to about 25 to 80°C., preferably to
`about 50 to 75° C., and most preferably to about 60 to 75° C.
`to form a first Solid phase and a first aqueous phase compris
`ing phospholipids and proteins; separating said first Solid
`phase from said first aqueous phase; and separating a protein
`and phospholipid fraction from said first aqueous phase. In
`some embodiments, the biomass is heated to the first tem
`perature for at least 3 minutes, preferably from about 3 min
`utes to 60 minutes, more preferably from about 3 minutes to
`20 minutes, and most preferably from about 3 minutes to 10
`minutes. The present invention is not limited to the use of any
`particular biological materials or biomass. In some embodi
`ments, the biological material is a marine biomass. In some
`preferred embodiments, the biological material or biomass
`comprises krill crabs, shrimp, calanus, plankton, crayfish,
`eggs or other phospholipid containing biological materials or
`biomass. The present invention is not limited to the use of any
`particular type of krill. In some embodiments, the krill is
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`fresh, while in other embodiments, the krill is frozen. In some
`embodiments, the krill is of the species Euphausia superba.
`In some embodiments, the step of separating a protein and
`phospholipid fraction from said first aqueous phase com
`prises heating said first aqueous phase at a temperature Suf
`ficient to form a phospholipid-protein coagulate and separat
`ing said phospholipid-protein coagulate from said aqueous
`phase. In some embodiments, the processes utilize a second
`heating step. In some embodiments, the first aqueous phase is
`heated to over 80°C., preferably to about 80 to 120° C., and
`most preferably to about 90 to 100°C. In some embodiments,
`the krill milk is held at these temperatures for from about 1
`minute to about 60 minutes, preferably about 1 minute to
`about 10 minutes, and most preferably for about 2 minutes to
`8 minutes. In some embodiments, the heating is at atmo
`spheric pressure, while in other embodiments, the pressure is
`greater than atmospheric pressure. In some embodiments, the
`processes further comprise the step of pressing said phospho
`lipid-protein coagulate to form a coagulate liquid phase and a
`coagulate press cake. In some embodiments, the processes
`further comprise drying said coagulate press cake to form a
`coagulate meal. In some embodiments, the processes further
`comprise extracting a coagulate oil from said coagulate meal.
`In some embodiments, the processes further comprise the
`steps of pressing and drying the coagulum to forma coagulum
`meal. In some embodiments, the drying is by hot air or steam.
`In some embodiments, the step of separating a protein and
`phospholipid fraction from said first aqueous phase com
`prises filtration of said aqueous phase to provide a phospho
`lipid-protein retentate comprising proteins and phospholip
`ids. In some embodiments, filtration is via membrane
`filtration. In some embodiments, the filtration comprises fil
`tering said aqueous phase through a microfilter with a pore
`size of from about 50 to 500 nm. In some embodiments, the
`processes further comprise the step of dewatering said phos
`pholipid-protein retentate to form a retentate liquid phase and
`a retentate concentrate. In some embodiments, the processes
`further comprise the step of removing water from said reten
`tate concentrate so that said retentate concentrate is microbi
`ally stable. In some embodiments, the processes further com
`prise the step of extracting a retentate oil from said retentate
`concentrate. In some embodiments, the processes further
`comprise the step of heating said first solid phase and then
`pressing said first solid phase to form a first press cake and a
`second liquid phase. In some embodiments, the processes
`further comprise the step of drying said first press cake to
`provide a first krill meal. In some embodiments, the processes
`further comprise the steps of heating said second liquid phase
`and then separating said second liquid phase to provide a first
`krill oil and stickwater. In some embodiments, the stickwater
`is evaporated and added to said first press cake, and a meal is
`formed from said evaporated Stickwater and said first press
`cake to provide a second krill meal. In some embodiments,
`the second liquid phase is heated to over 80°C., preferably to
`about 80 to 120° C., and most preferably to about 90 to 100°
`C. prior to said separation. In some embodiments, the pro
`cesses further comprise the step of combining the previously
`described coagulate oil or the retentate oil and the first krill oil
`to provide a blended oil. In other embodiments, the coagulate
`oil, retentate oil, or oil pressed from the first solid phase are
`combined with the coagulate meal or retentate. In further
`embodiments, the processes of the present invention com
`prise the further step of Supplementing the meals or oils
`produced as described above with additional proteins, phos
`pholipids, triglycerides, fatty acids, and/or astaxanthin to pro
`duce an oil or meal with a desired defined composition. As
`such, a person of skill in the art will readily recognize that the
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