The present invention relates to a process for treating an oil comprising a chlorophyll derivative. In particular, the present disclosure relates to an improved process for removing impurities, including chlorophyll derivatives and/or trace metals, from an oil using an adsorbent comprising a silica treated with an alkali earth metal oxide, such as magnesium oxide. The process comprises contacting the oil with the adsorbent, wherein the pH of the silica is about 7 or greater, including from about 7 to about 10. The process may further comprise contacting the oil with a polypeptide having decolorase activity or a composition comprising the polypeptide, prior to contact with the adsorbent.
B01J 20/10 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtration; Absorbants ou adsorbants pour la chromatographie; Procédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant de la silice ou un silicate
The present invention relates to a process for treating an oil comprising a chlorophyll derivative. In particular, the present disclosure relates to an improved process for removing impurities, including chlorophyll derivatives and/or trace metals, from an oil using an adsorbent comprising a silica treated with an alkali earth metal oxide, such as magnesium oxide. The process comprises contacting the oil with the adsorbent, wherein the pH of the silica is about 7 or greater, including from about 7 to about 10. The process may further comprise contacting the oil with a polypeptide having decolorase activity or a composition comprising the polypeptide, prior to contact with the adsorbent.
The present invention relates to a process for treating an oil comprising a chlorophyll derivative. In particular, the present disclosure relates to an improved process for removing impurities, including chlorophyll derivatives and/or trace metals, from an oil using an adsorbent comprising a silica treated with an alkali earth metal oxide, such as magnesium oxide. The process comprises contacting the oil with the adsorbent, wherein the pH of the silica is about 7 or greater, including from about 7 to about 10. The process may further comprise contacting the oil with a polypeptide having decolorase activity or a composition comprising the polypeptide, prior to contact with the adsorbent.
B01J 20/10 - Compositions absorbantes ou adsorbantes solides ou compositions facilitant la filtration; Absorbants ou adsorbants pour la chromatographie; Procédés pour leur préparation, régénération ou réactivation contenant une substance inorganique contenant de la silice ou un silicate
The present disclosure provides for improved oilseed extraction methods using sequential extractions with polar solvents and non-polar solvents or extractions with an azeotrope of a polar solvent and a non-polar solvent to produce oilseed meal concentrates having increased protein content and reduced soluble carbohydrate and anti-nutritional compound content.
C11B 1/10 - Production des graisses ou huiles à partir de matières premières par extraction
A23L 5/20 - Préparation ou traitement des aliments ou produits alimentaires en général; Aliments ou produits alimentaires ainsi obtenus; Leurs matériaux Élimination de constituants indésirables, p.ex. désodorisation ou détoxication
A23L 11/00 - Légumes secs, c. à d. fruits de plantes légumineuses, pour l'obtention d'aliments; Produits dérivés de légumineuses; Leur préparation ou leur traitement
A23L 11/30 - Légumes secs, c. à d. fruits de plantes légumineuses, pour l'obtention d'aliments; Produits dérivés de légumineuses; Leur préparation ou leur traitement Élimination des substances indésirables, p.ex. des substances amères
The present disclosure provides for improved oilseed extraction methods using sequential extractions with polar solvents and non-polar solvents or extractions with an azeotrope of a polar solvent and a non-polar solvent to produce oilseed meal concentrates having increased protein content and reduced soluble carbohydrate and anti-nutritional compound content.
C11B 1/10 - Production des graisses ou huiles à partir de matières premières par extraction
A23L 5/20 - Préparation ou traitement des aliments ou produits alimentaires en général; Aliments ou produits alimentaires ainsi obtenus; Leurs matériaux Élimination de constituants indésirables, p.ex. désodorisation ou détoxication
A23L 11/00 - Légumes secs, c. à d. fruits de plantes légumineuses, pour l'obtention d'aliments; Produits dérivés de légumineuses; Leur préparation ou leur traitement
A23L 11/30 - Légumes secs, c. à d. fruits de plantes légumineuses, pour l'obtention d'aliments; Produits dérivés de légumineuses; Leur préparation ou leur traitement Élimination des substances indésirables, p.ex. des substances amères
Methods for reducing the color of phospholipid compositions comprising lecithin are disclosed. The phospholipid composition is exposed to ultraviolet light to reduce the color of the composition. The phospholipid composition may be diluted and/or heated prior to exposure to ultraviolet light to improve the flow properties of the composition. The phospholipid composition may be cooled and/or concentrated after color reduction.
Methods for reducing the color of phospholipid compositions comprising lecithin are disclosed. The phospholipid composition is exposed to ultraviolet light to reduce the color of the composition. The phospholipid composition may be diluted and/or heated prior to exposure to ultraviolet light to improve the flow properties of the composition. The phospholipid composition may be cooled and/or concentrated after color reduction.
A23L 5/40 - Coloration ou décoloration des aliments
A23D 9/02 - Autres huiles ou graisses comestibles, p.ex. huiles pour cuisson caractérisées par leur production ou leur traitement
B01J 19/12 - Procédés utilisant l'application directe de l'énergie ondulatoire ou électrique, ou un rayonnement particulaire; Appareils à cet usage utilisant des radiations électromagnétiques
Methods for reducing the color of phospholipid compositions comprising lecithin are disclosed. The phospholipid composition is exposed to ultraviolet light to reduce the color of the composition. The phospholipid composition may be diluted and/or heated prior to exposure to ultraviolet light to improve the flow properties of the composition. The phospholipid composition may be cooled and/or concentrated after color reduction.
The present invention relates to a process for treating an oil comprising a chlorophyll substrate, the process comprising contacting the oil with a polypeptide having decolorase activity or a composition comprising the polypeptide, wherein the polypeptide is selected from the group consisting of: a. a polypeptide which has at least 80% identity to amino acids 1 to 318 of SEQ ID NO: 1; and, b. a polypeptide encoded by a nucleic acid sequence that has at least 80% identity to the nucleic acid sequence of SEQ ID NO: 2.
The present invention relates to a process for treating an oil comprising a chlorophyll substrate, the process comprising contacting the oil with a polypeptide having decolorase activity or a composition comprising the polypeptide, wherein the polypeptide is selected from the group consisting of: a. a polypeptide which has at least 80% identity to amino acids 1 to 318 of SEQ ID NO: 1; and, b. a polypeptide encoded by a nucleic acid sequence that has at least 80% identity to the nucleic acid sequence of SEQ ID NO: 2.
Provided here is an enzymatic process for extraction of oil from algae biomass. The oils produced by the processes herein are used in animal feed and human consumption.
C11B 1/10 - Production des graisses ou huiles à partir de matières premières par extraction
C12P 7/64 - Graisses; Huiles; Cires de type ester; Acides gras supérieurs, c. à d. ayant une chaîne continue d'au moins sept atomes de carbone liée à un groupe carboxyle; Huiles ou graisses oxydées
Provided here is an enzymatic process for extraction of oil from algae biomass. The oils produced by the processes herein are used in animal feed and human consumption.
C12P 7/64 - Graisses; Huiles; Cires de type ester; Acides gras supérieurs, c. à d. ayant une chaîne continue d'au moins sept atomes de carbone liée à un groupe carboxyle; Huiles ou graisses oxydées
A process for preparing a sunflower meal fraction containing at least 50% of proteins and 10% or less of crude fibers. Sunflower meal fraction obtained by the process thereof and its use for preparing animal feed compositions.
A23J 1/14 - Préparation des compositions à base de protéines pour l'alimentation; Ouverture des œufs par grandes quantités et séparation du jaune du blanc à partir des tourteaux ou des graines oléagineuses
A23K 1/14 - à partir de matières végétales, p.ex. de pommes de terre ou de racines, sans ensilage
A23K 1/16 - additionnés d'éléments nutritifs accessoires; Blocs de sel
In alternative embodiments, the invention provides phosphatidylinositol-specific phospholipase C (PI-PLC) enzymes, nucleic acids encoding them, antibodies that bind specifically to them, and methods for making and using them. Industrial methods and products comprising use of these phospholipases are also provided. In certain embodiments, provided herein are methods for hydration of non hydratable phospholipids (NHPs) within a lipid matrix. The methods enable migration of NHPs to an oil-water interface thereby allowing the NHPs to be reacted and/or removed from the lipids. In certain embodiments, provided is a method for removing NHPs, hydratable phospholipids, and lecithins from vegetable oils to produce a degummed oil or fat product that can be used for food production and/or non-food applications. In certain embodiments, provided herein are methods for hydration of NHPs followed by enzymatic treatment and removal of various phospholipids and lecithins. The methods provided herein can be practiced on either crude or water-degummed oils.
C12P 7/64 - Graisses; Huiles; Cires de type ester; Acides gras supérieurs, c. à d. ayant une chaîne continue d'au moins sept atomes de carbone liée à un groupe carboxyle; Huiles ou graisses oxydées
Provided here is an enzymatic process for production of low saturate oil, in one embodiment, low palmitic oils from triacvlglycerol sources. The enzymes used in the processes herein are saturase enzymes, including palmitase enzymes. The oils produced by the processes herein are used in food products.
Provided here is an enzymatic process for production of low saturate oil, in one embodiment, low palmitic oils from triacylglycerol sources. The enzymes used in the processes herein are saturase enzymes, including palmitase enzymes. The oils produced by the processes herein are used in food products.
C12P 7/64 - Graisses; Huiles; Cires de type ester; Acides gras supérieurs, c. à d. ayant une chaîne continue d'au moins sept atomes de carbone liée à un groupe carboxyle; Huiles ou graisses oxydées
G11B 3/00 - Enregistrement par gravure, déformation ou pressage mécaniques, p.ex. de sillons ou de creux; Reproduction par lecture mécanique; Supports d'enregistrement correspondants
C11C 1/04 - Préparation des acides gras à partir de graisses, huiles ou cires; Raffinage des acides gras à partir de graisses ou huiles par hydrolyse
Provided here is an enzymatic process for production of low saturate oil, in one embodiment, low palmitic oils from triacvlglycerol sources. The enzymes used in the processes herein are saturase enzymes, including palmitase enzymes. The oils produced by the processes herein are used in food products.
Foodstuffs for animals, namely, processed food material for the composition of final food compound for animals, not including pet food for domestic animals
In alternative embodiments, the invention provides phosphatidylinositol-specific phospholipase C (PI-PLC) enzymes, nucleic acids encoding them, antibodies that bind specifically to them, and methods for making and using them. Industrial methods and products comprising use of these phospholipases are also provided. In certain embodiments, provided herein are methods for hydration of non hydratable phospholipids (NHPs) within a lipid matrix. The methods enable migration of NHPs to an oil-water interface thereby allowing the NHPs to be reacted and/or removed from the lipids. In certain embodiments, provided is a method for removing NHPs, hydratable phospholipids, and lecithins from vegetable oils to produce a degummed oil or fat product that can be used for food production and/or non-food applications. In certain embodiments, provided herein are methods for hydration of NHPs followed by enzymatic treatment and removal of various phospholipids and lecithins. The methods provided herein can be practiced on either crude or water-degummed oils.
C10L 1/02 - Combustibles carbonés liquides à base essentielle de composants formés uniquement de carbone, d'hydrogène et d'oxygène
C12P 7/64 - Graisses; Huiles; Cires de type ester; Acides gras supérieurs, c. à d. ayant une chaîne continue d'au moins sept atomes de carbone liée à un groupe carboxyle; Huiles ou graisses oxydées
27.
PROCESS FOR AQUEOUS OIL EXTRACTION FROM OILSEED STARTING MATERIAL
A process is disclosed for the efficient recovery of oil from oilseed materials without the use of organic solvents. In the process, the oilseed starting material is first expelled to remove a portion of the total oil. The expelled cake retains the remainder of the oil from the starting seed. This cake is slurried in water and the pH of the slurry is adjusted to pH > 8 with an alkaline compound. This pH adjustment results in release of oil from binding to other compounds and structures in the slurry. The slurry is then processed through a solids-liquid separation to produce a protein-enriched solids phase and an oil-in- water liquid phase. The liquid phase is then further processed to separate the oil from the water and recover the oil as free oil. The recovered oil can then be added to the expelled oil.
C11B 1/10 - Production des graisses ou huiles à partir de matières premières par extraction
A23D 9/00 - Autres huiles ou graisses comestibles, p.ex. huiles pour cuisson
A23J 1/14 - Préparation des compositions à base de protéines pour l'alimentation; Ouverture des œufs par grandes quantités et séparation du jaune du blanc à partir des tourteaux ou des graines oléagineuses
Shown is a two stage filtration system for treatment of fibrous vegetable matter, particularly oilseed materials such as oil-extracted canola flakes to separate the low valued fibrous material from soluble material and small non-structural water-insoluble material of higher value. The filtration system receives a vegetable matter slurry and passes the slurry through first stage filter which is an impeller type filter that operates to separate the slurry into a filtrate and a moist retentate. The moist retentate is further filter in a second compression filtration stage or a centrifuge to remove additional water. Small non-structural insoluble matter is removed in the filtrate.
