EP1978818A2 - Procédé pour obtenir une fraction de protéine végétale, notamment pour confectionner une crème glacée végétale - Google Patents

Procédé pour obtenir une fraction de protéine végétale, notamment pour confectionner une crème glacée végétale

Info

Publication number
EP1978818A2
EP1978818A2 EP07702345A EP07702345A EP1978818A2 EP 1978818 A2 EP1978818 A2 EP 1978818A2 EP 07702345 A EP07702345 A EP 07702345A EP 07702345 A EP07702345 A EP 07702345A EP 1978818 A2 EP1978818 A2 EP 1978818A2
Authority
EP
European Patent Office
Prior art keywords
vegetable
proteins
mixture
substances
protein
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP07702345A
Other languages
German (de)
English (en)
Inventor
Peter Eisner
Klaus Müller
Claudia Pickardt
Andreas Malberg
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fraunhofer Gesellschaft zur Forderung der Angewandten Forschung eV
Original Assignee
Fraunhofer Gesellschaft zur Forderung der Angewandten Forschung eV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Application filed by Fraunhofer Gesellschaft zur Forderung der Angewandten Forschung eV filed Critical Fraunhofer Gesellschaft zur Forderung der Angewandten Forschung eV
Publication of EP1978818A2 publication Critical patent/EP1978818A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
    • A23G9/32—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds
    • A23G9/38—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds containing peptides or proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23G—COCOA; COCOA PRODUCTS, e.g. CHOCOLATE; SUBSTITUTES FOR COCOA OR COCOA PRODUCTS; CONFECTIONERY; CHEWING GUM; ICE-CREAM; PREPARATION THEREOF
    • A23G9/00—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor
    • A23G9/32—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds
    • A23G9/42—Frozen sweets, e.g. ice confectionery, ice-cream; Mixtures therefor characterised by the composition containing organic or inorganic compounds containing plants or parts thereof, e.g. fruits, seeds, extracts
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/006—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from vegetable materials
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
    • A23J1/14—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from leguminous or other vegetable seeds; from press-cake or oil-bearing seeds
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
    • A23J3/00—Working-up of proteins for foodstuffs
    • A23J3/14—Vegetable proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/10—Foods or foodstuffs containing additives; Preparation or treatment thereof containing emulsifiers
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs

Definitions

  • Protein fraction in particular for the production of vegetable ice cream
  • the present invention relates to a process for obtaining a vegetable protein fraction, in particular for producing vegetable ice cream, in which plant parts are mixed with water or a water-containing solvent in order to dissolve and / or disperse vegetable proteins from the plant parts, and in which one or more vegetable protein fractions are separated from the water-containing mixture thus obtained by a separation process.
  • Ice cream and other creamy ice cream variants contain animal or vegetable fats and
  • Milk protein and / or milk sugar as well as partially egg protein fulfill in the ice cream in addition to a possibly desirable taste in particular functions of texturing.
  • the manufacture of ice cream is essentially performed by weighing the ingredients, pre-mixing, homogenizing, pasteurizing, cooling (+4 0 C), ripening, freezing in the ice freezing Let anläge (Freezen), packaging and storage.
  • Ice cream such as mousse is known (at least 50% milk content and one liter Milk at least 270 g whole egg or 90 g egg yolks), cream ice cream (at least 18% milk fat from whipped cream), ice cream (at least 10% milk fat), simple ice cream (at least 3% milk fat), milk ice (milk content at least 70%) and ice cream with vegetable fat (at least 3% vegetable fat).
  • cream ice cream at least 50% milk content and one liter Milk at least 270 g whole egg or 90 g egg yolks
  • cream ice cream at least 18% milk fat from whipped cream
  • ice cream at least 10% milk fat
  • simple ice cream at least 3% milk fat
  • milk ice milk content at least 70%
  • ice cream with vegetable fat at least 3% vegetable fat.
  • Common to all these ice creams is that they contain milk protein and lactose in addition to animal or vegetable fats.
  • the creaminess is of particular importance.
  • the creaminess is determined by the fat content and its integration into the total matrix.
  • the viscosity of the melt determines the creaminess of the ice. A higher viscosity melt is perceived as creamier in the mouth than a low viscosity melt.
  • the melting behavior determines the organoleptic sensation during the consumption of ice. An ice cream with a slow, uniform melting behavior is perceived as more pleasant than an ice cream with a heterogeneous and z.T. very fast absorption behavior.
  • the breakdown behavior is influenced inter alia by the impact, i. the volume-related
  • Gas content air or nitrogen determined in the ice. Most creamy types of ice cream have a gas content of over 40 to 50 vol .-%. Such a service So far, it can only be achieved with conventional ingredients.
  • Creamy types of ice cream are obtainable in the prior art only by larger amounts of fat, to achieve the Kremtechniks 1977s the fat content should be greater than 15 wt .-%, better than 20% by weight.
  • Plants used to obtain proteins for use in ice cream contain between 10% and 50% by weight protein in the dry matter, depending on the feedstock.
  • the protein content in plants does not consist of a defined substance.
  • the total protein includes a variety of different protein fractions. Each protein fraction is from several hundred to more than - A -
  • individual protein fractions have particularly good properties as emulsifier or gelling agent, as water binders, foaming agents or texture improvers for foods.
  • emulsifier or gelling agent as water binders, foaming agents or texture improvers for foods.
  • Protein mix e.g. is obtained by drying a protein solution.
  • the extraction of vegetable protein products is so far almost exclusively from soybeans.
  • the beans are peeled, further comminuted by flocculation or grinding and the protein extracted by adding water from the soy flakes or the flour.
  • the aqueous extract can be removed by mechanical separation techniques from the undissolved solids, e.g. Fibers are separated and routed out of the extraction process.
  • the soy protein product can then be precipitated from the extract, enriched with membrane processes and / or dried.
  • the proteins are obtained as a protein product although they consist of different protein fractions with different properties.
  • a separation of the protein fractions according to emulsifier specific, functional properties is not carried out according to the prior art. Rather, fractionation is after material sum parameters such as precipitability, solubility or molecular size.
  • Another method for the separation of protein-containing suspensions and solutions are filtration or membrane processes. So can be separated by simple filtration suspended from dissolved proteins. It is also possible to use molecules of different sizes, e.g. by ultrafiltration into a fraction of larger and to separate into a fraction of smaller molecules. The specific properties of the fractions obtained can only be adapted to a limited extent to the requirements of the food industry. In many cases, the larger and precipitable molecular fractions have better properties than emulsifiers, while the smaller or non-precipitable fraction has better properties than foaming agents.
  • WO 2006/076889 A2 a process for the preparation of a vegetable protein ingredient for an ice cream is described.
  • Lupine seeds are prepared and first crushed. Thereafter, in one or more protein extraction steps, a portion of one in the comminuted lupine seeds - S -
  • lupine protein dissolved or at least dispersed in an aqueous phase.
  • the lupine protein is separated by precipitation from the aqueous phase.
  • the object of the present invention is to provide a method for obtaining a vegetable protein fraction with particularly good emulsifying properties, which can be used particularly advantageous as an emulsifier in the production of vegetable ice cream.
  • plant parts in particular peeled or unshelled plant seeds, are mixed with water or a water-containing solvent in order to dissolve and / or disperse vegetable proteins from the plant parts.
  • one or more substances with lipophilic or amphiphilic interfaces are introduced into the mixture obtained in this way or brought into contact with the mixture, in which in the mixture dissolved and / or dispersed proteins with lipophilic or amphiphilic groups, hereinafter also as target proteins designated, attach.
  • the one or more substances with the attached proteins are separated from the mixture by a separation process to obtain the desired vegetable protein fraction (s).
  • the fractionation of the mixture of different dissolved and / or dispersed protein fractions present in water or a water-containing solution thus takes place by introducing a lipophilic or amphiphilic phase boundary into the water or into the mixture.
  • Proteins with a high affinity for lipophilic substances attach themselves to the lipophilic interfaces and can thus be separated from other dissolved or dispersed substances.
  • the process thus enables a selective recovery of surface-active emulsifier protein, which attaches to the lipophilic or amphiphilic interfaces due to its lipophilic or amphiphilic properties.
  • This protein fraction obtained by the process is of great advantage in enriched form, above all for the production of vegetable ice cream, to which it is preferably added in a proportion of between 0.5 and 6% by weight.
  • the selective fractionation of the proteins into a particularly efficient emulsifier protein fraction made possible by the present process makes it possible to produce ice cream with particularly positive properties and appealing organoleptic properties.
  • a substance is used, due to the lipophilic structure of the interface advantageous to attach lipophilic groups of proteins.
  • lipophilic surfaces of polymers or other adsorber materials which, for example, are brought into contact with the protein mixture as a fixed bed or as dispersed particles.
  • Fractionation protein fractions are obtained whose emulsifying capacity (binding capacity of oil in water) per gram of protein by a factor of 5 compared to the original protein mixture is increased. The amount of additional emulsifier required for different applications can thus be reduced to a minimum.
  • oil droplets or fat particles are used as substance with lipophilic interface or surface.
  • the proteins with pronounced lipophilic properties attach to this surface, whereas proteins with less pronounced lipophilic properties do not or only to a small extent attach to the phase interface.
  • Other substances with low lipophilic intrinsic properties which are present in the mixture, e.g. Saccharides, salts or fibers do not or only to a small extent attach to the lipophilic surfaces.
  • the proposed method very efficiently succeeds in separating proteins with a defined ratio of lipophilic and hydrophilic properties from other dissolved or dispersed proteins.
  • By adapting the surface properties Shafts for example by the selection of different polymers with different polar and non-polar groups on the surface, succeeds in selecting the proteins.
  • proteins also always have hydrophilic regions in addition to the lipophilic group, the process according to the invention allows fractionation of the proteins according to their ratio of lipophilic groups to hydrophilic groups, depending on the lipophilic characteristics of the interface.
  • the properties of the respective protein obtained can be specifically optimized for use in different applications, for example for the production of vegetable ice cream.
  • the remaining aqueous mixture is separated from the lipophilic substances with the attached proteins.
  • the aqueous phase can be mechanically separated. Besides filtration, centrifugal processes are suitable for this purpose. A prerequisite for a good separation is that the lipophilic particles or droplets have a different density than the surrounding aqueous mixture.
  • lipophilic adsorbents often have a comparable or somewhat lower density than water, floating of the lipophilic substances together with the attached proteins can be achieved.
  • the aqueous phase can be enriched for this with soluble salts or with sugar, which increases the specific gravity of the liquid phase. result.
  • the lighter lipophilic substances can be separated together with the attached proteins as a floating fraction of the liquid and discharged, for example by means of decanters.
  • a vegetable oil or fat is added to the aqueous protein mixture as the lipophilic substance or phase.
  • the lipophilic target proteins are deposited and can be separated from the aqueous phase by centrifugation.
  • the vegetable oil used is preferably the oil which is to be used in the food later as an oil phase in the emulsion.
  • rapeseed oil droplets if appropriate also together with further constituents of the rapeseed, can be used as lipophilic phase boundary surface in the aqueous protein mixture for the fractionation.
  • the by fractionation obtained Raps ⁇ l protein mixture can then be used directly as an ingredient for the vegetable ice cream.
  • ice cream in which other vegetable oils are used. Possibly. may be added to the oil before use as a lipophilic substance certain substances that are desirable in the subsequent preparation. Thus, flavors, colors, vitamins, phytochemicals or other bioactive substances may be added. In ice cream, these substances are then present in a defined concentration.
  • the phase boundary is produced directly with the oil from the protein-containing plant.
  • soybean oil from soybean can be used to fractionate soya proteins.
  • oil droplets with a droplet size ⁇ 100 .mu.m, preferably ⁇ 10 .mu.m are produced here with the mixing or comminution device.
  • the greater amount of intermingling fluid between the smaller oil droplets also removes more dissolved proteins that do not have the specific properties of interfacially attached proteins. In this case it is it is helpful to separate the graft fluid in one or more washing stages from the emulsifier proteins adhering to the oil droplets.
  • a person skilled in the art is able, depending on the desired protein purity, to set the required droplet size by selecting the stirring or ultrasound conditions and to use the required number of washing steps, which gives the best results for the desired protein purity.
  • emulsifier proteins are obtained when using oil-containing plants such as rapeseed, palm kernels, flax or sunflower.
  • oil-containing plants such as rapeseed, palm kernels, flax or sunflower.
  • other oily plants such as e.g. Soy or Lupine to use for the said application.
  • the oil serves as an absorber surface and is not separated from the protein after protein fractionation.
  • the moist oil-protein mixture is then incorporated particularly advantageously directly into the ice cream.
  • the ice is enriched with vegetable oil and there is a particularly stable ice cream emulsion in which even after prolonged storage in the frozen state no organoleptically perceptible oxidative changes occur.
  • the proteins remain in their dissolved, native structure.
  • the complete separation of the water eg by means of drying, would change the proteins and thus impair the ice quality.
  • the phase interface is not produced with vegetable oil but with other adsorbers, such as polymers, the proteins must subsequently be separated from the adsorbers.
  • water, emulsions or lipophilic liquids such as hexane, acetone, alcohols or other solvents are suitable. From these liquids, the protein may optionally be recovered in pure form by the liquid is separated from the protein again. In the case of solvents, evaporation can take place.
  • a pure protein can also be obtained when the protein is separated from the aqueous mixture along with oil droplets. After drying the water, the resulting oil-protein mixture can be mixed with a lipophilic solvent, e.g. Hexane or acetone or others, whereby the oil phase is removed and the protein is recovered in pure form.
  • a lipophilic solvent e.g. Hexane or acetone or others
  • Ice cream is also used in other foods.
  • hydrophilic protein fractions After removal of the lipophilic protein fraction hydrophilic protein fractions remain in solution in the aqueous mixture. These may be concentrated by isoelectric precipitation or filtration techniques and recovered as a protein isolate characterized in particular by high water solubility, foam-forming properties, gelation and viscosity-forming properties.
  • This hydrophilic protein product can be advantageously used in the production of beverages, foamed foods such as chocolate kiss, water and milk-based desserts or baked goods.
  • hydrophilic protein fraction it is also possible to carry out various pretreatment steps with more or less lipophilic adsorbers in the aqueous protein mixture.
  • further fractions can be separated off and the properties of the proteins discharged with the adsorbers and the proteins remaining in the mixture can be further specialized.
  • By combining different adsorbers it is possible to obtain distinctively hydrophilic proteins in a highly pure form as the end product.
  • Example 1 Creamy vegetable ice with reduced fat content
  • the insoluble constituents predominantly fibers and shell residues, are separated from the protein-oil-water dispersion through a 63 ⁇ m sieve.
  • the emulsion phase is obtained after centrifuging the filtrate by ablating the upper layer.
  • the heavier liquid phase after centrifugation contains, in contrast to the emulsion phase, the less well-emulsifying, but particularly readily water-soluble proteins and can be further worked up to obtain them. So these proteins z. B. be obtained by ultrafiltration.
  • the solid filter residue is washed once more with 200 g of sugar solution and so won a further share of emulsifier proteins together with the remaining oil and other soluble constituents.
  • the combined emulsion phase (82 g) containing the emulsifier proteins together with the sunflower oil is mixed with 400 g of water to separate impurities such as soluble non-emulsifier proteins.
  • the mixture is then centrifuged.
  • the emulsifier proteins remain bound to the oil and can thus be separated as a floating phase.
  • This emulsion phase is again washed with water in the same manner to separate unwanted soluble constituents.
  • the desired water or oil content of the emulsion is adjusted by the addition of water.
  • the emulsion prepared is used according to the recipe given in Table 1 for the production of ice cream.
  • the emulsion already has a fat content, so that an additional addition of vegetable fat is eliminated. It is a particularly creamy pure vegetable ice cream is achieved, but has a very low fat content of only 8%.
  • the fat is emulsified so well that even with a long storage time of 6 months, no large ice crystals are formed in the ice. Thus, the ice is also very stable and stays creamy for a long time.
  • Table 1 Formulation for the production of vegetable ice cream
  • Example 2 Vegetable ice cream with ice-cream character
  • Example 1 The emulsion of Example 1 is incorporated in exchange for cream in a cream-ice cream recipe. Due to the good emulsifier effect of the protein can be dispensed with the addition of artificial emulsifiers. The stability of the emulsion is also very good in this "ice cream", good storage stability is given.

Abstract

L'invention concerne un procédé pour obtenir une fraction de protéine végétale, notamment pour confectionner une crème glacée végétale, procédé selon lequel des fragments végétaux sont mélangés à de l'eau ou à un solvant aqueux pour détacher et/ou disperser des protéines végétales de ces fragments végétaux. Selon le procédé, une ou plusieurs fractions de protéine végétale sont séparées au moyen d'un procédé de séparation du mélange aqueux obtenu. Selon l'invention, pour séparer la ou les fractions de protéine végétale, une ou plusieurs substances à interfaces lipophiles ou amphiphiles sont introduites dans le mélange, et les protéines à groupes lipophiles ou amphiphiles qui ont été séparées et/ou dispersées dans le mélange se fixent sur ces substances. Lesdites substances, avec les protéines ainsi fixées, sont alors séparées du mélange. Le procédé de l'invention permet d'obtenir une fraction de protéine végétale présentant des propriétés émulsifiantes particulièrement bonnes, cette fraction de protéine étant particulièrement adaptée comme émulsifiant lors de la confection de crème glacée végétale.
EP07702345A 2006-01-17 2007-01-17 Procédé pour obtenir une fraction de protéine végétale, notamment pour confectionner une crème glacée végétale Withdrawn EP1978818A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102006002249A DE102006002249B4 (de) 2006-01-17 2006-01-17 Verfahren zur Gewinnung einer pflanzlichen Proteinfraktion, insbesondere zur Herstellung von pflanzlichem Speiseeis
PCT/DE2007/000064 WO2007082507A2 (fr) 2006-01-17 2007-01-17 Procédé pour obtenir une fraction de protéine végétale, notamment pour confectionner une crème glacée végétale

Publications (1)

Publication Number Publication Date
EP1978818A2 true EP1978818A2 (fr) 2008-10-15

Family

ID=38162185

Family Applications (1)

Application Number Title Priority Date Filing Date
EP07702345A Withdrawn EP1978818A2 (fr) 2006-01-17 2007-01-17 Procédé pour obtenir une fraction de protéine végétale, notamment pour confectionner une crème glacée végétale

Country Status (8)

Country Link
US (1) US8257772B2 (fr)
EP (1) EP1978818A2 (fr)
KR (1) KR20080083318A (fr)
CN (1) CN101374418A (fr)
CA (1) CA2634350A1 (fr)
DE (1) DE102006002249B4 (fr)
NO (1) NO336729B1 (fr)
WO (1) WO2007082507A2 (fr)

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US8142822B2 (en) * 2008-06-20 2012-03-27 Burcon Nutrascience (Mb) Corp. Canola protein isolate
US9056894B2 (en) * 2010-10-27 2015-06-16 Philip Morris Products S.A. Methods for capturing virus like particles from plants using expanded bed chromatogrpahy
EP2814330A1 (fr) * 2012-02-15 2014-12-24 Burcon Nutrascience (MB) Corp. Mélanges de dessert congelés utilisant des produits à base de protéine de canola
EP2869713A1 (fr) * 2012-07-09 2015-05-13 Burcon Nutrascience (MB) Corp. Mélanges de dessert congelés utilisant des produits de protéine de légumineuse
DE102015201069A1 (de) * 2014-02-14 2015-08-20 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Instantmischung, insbesondere für Softeis, und Verfahren zur Herstellung
WO2017001266A1 (fr) * 2015-06-30 2017-01-05 Unilever Plc Confiserie glacée à base de protéines végétales
WO2017001265A1 (fr) 2015-06-30 2017-01-05 Unilever Plc Confiserie congelée
EP3123871A1 (fr) 2015-07-30 2017-02-01 Lupino AG Deutschland Extraction mécanique de protéine de lupin
CN105211493B (zh) * 2015-10-26 2019-06-11 济南大学 一种复合植物蛋白营养冰淇淋及其制备方法
BE1024164B1 (nl) * 2016-09-19 2017-11-23 Alpro, Commanditaire Vennootschap Op Aandelen Plantaardig calorie-arm ijsproduct en methode om deze te vervaardigen
KR20230145043A (ko) * 2020-11-30 2023-10-17 어패로 엘엘씨 오일 종자로부터의 추출물 및 오일 종자를 가공하는방법

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GB9807256D0 (en) 1998-04-03 1998-06-03 Du Pont Uk Functional protein compositions,emulsions based thereon and processes for their preparation
EP1405572A1 (fr) * 2002-10-04 2004-04-07 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Protéines de lupin modifiées pour la préparation d'une formulation de produit hydro-dispersable d'un composant soluble dans la graisse
NZ542956A (en) * 2003-03-21 2007-11-30 Upfront Chromatography As Method for high throughput volumes in the fractionation of bio-molecules by chromatographic systems
AU2003901942A0 (en) * 2003-04-24 2003-05-15 The State Of Western Australia Through Its Department Of Agriculture Lupin protein-based dairy substitute production
EP1838161B1 (fr) * 2005-01-18 2015-05-27 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Procede de production d'un complement proteique vegetal d'une glace et glace contenant ce complement proteique

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Also Published As

Publication number Publication date
US20090011107A1 (en) 2009-01-08
WO2007082507A2 (fr) 2007-07-26
DE102006002249A1 (de) 2007-07-26
KR20080083318A (ko) 2008-09-17
DE102006002249B4 (de) 2010-12-09
CN101374418A (zh) 2009-02-25
WO2007082507A3 (fr) 2007-09-13
NO20082738L (no) 2008-07-23
CA2634350A1 (fr) 2007-07-26
NO336729B1 (no) 2015-10-26
US8257772B2 (en) 2012-09-04

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