EP2475268A2 - Utilisation de graines de colza décortiquées - Google Patents

Utilisation de graines de colza décortiquées

Info

Publication number
EP2475268A2
EP2475268A2 EP10810743A EP10810743A EP2475268A2 EP 2475268 A2 EP2475268 A2 EP 2475268A2 EP 10810743 A EP10810743 A EP 10810743A EP 10810743 A EP10810743 A EP 10810743A EP 2475268 A2 EP2475268 A2 EP 2475268A2
Authority
EP
European Patent Office
Prior art keywords
rapeseed
powder
basic
filling
oil
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Withdrawn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
EP10810743A
Other languages
German (de)
English (en)
Inventor
Michael Rass
Christian Schein
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.)
Teutoburger Olmuehle & Co KG GmbH
Original Assignee
Teutoburger Olmuehle & Co KG GmbH
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
Application filed by Teutoburger Olmuehle & Co KG GmbH filed Critical Teutoburger Olmuehle & Co KG GmbH
Publication of EP2475268A2 publication Critical patent/EP2475268A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • 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
    • A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/10—Natural spices, flavouring agents or condiments; Extracts thereof
    • A23L27/14—Dried spices
    • A—HUMAN NECESSITIES
    • A21—BAKING; EDIBLE DOUGHS
    • A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
    • A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
    • A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
    • A21D2/24—Organic nitrogen compounds
    • A21D2/26—Proteins
    • A21D2/264—Vegetable proteins
    • A21D2/266—Vegetable proteins 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
    • 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
    • A23L13/00—Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/20—Meat products; Meat meal; Preparation or treatment thereof from offal, e.g. rinds, skins, marrow, tripes, feet, ears or snouts
    • 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
    • A23L13/00—Meat products; Meat meal; Preparation or treatment thereof
    • A23L13/40—Meat products; Meat meal; Preparation or treatment thereof containing additives
    • A23L13/42—Additives other than enzymes or microorganisms in meat products or meat meals
    • A23L13/426—Addition of proteins, carbohydrates or fibrous material from vegetable origin other than sugars or sugar alcohols
    • 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
    • A23L25/00—Food consisting mainly of nutmeat or seeds; Preparation or treatment thereof
    • A23L25/30—Mashed or comminuted products, e.g. pulp, pastes, meal, powders; Products made therefrom, e.g. blocks, flakes, snacks; Liquid or semi-liquid products
    • 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
    • A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
    • A23L27/10—Natural spices, flavouring agents or condiments; Extracts thereof
    • 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
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/105—Plant extracts, their artificial duplicates or their derivatives
    • 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
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/17—Amino acids, peptides or proteins
    • A23L33/185—Vegetable proteins

Definitions

  • the invention relates to a method for processing rapeseed, which are peeled and separated into cores (parenchymal tissue and radicle) on the one hand and shell portions on the other hand and wherein the cores are subjected to one or more pressings for oil production, while a solid and oil-containing press cake remains
  • cores parenchymal tissue and radicle
  • the invention is based on the problem to achieve a high-quality use of press cake in rapeseed processing.
  • the invention solves this problem by a method having the features of claim 1 and by a novel use according to claim 10 or 11 and by a powder having the features of claim 12.
  • a powder having the features of claim 12. is based on the dependent claims 2 to 9 and 13 referenced.
  • the squeezed out oil can be used as food, but also a remaining presscake as a high-quality, protein-containing basic, filling or addition substance for pet food, so that the total utilization rate of rapeseed increases considerably.
  • the flowability of the resulting powder is particularly advantageous in the further processing into pellets by extrusion or mixing and extrusion process used.
  • the further grinding process may comprise a cryogenic grinding, so that even with a relatively high residual oil content in the supplied millbase grinding without sticking involved in the grinding process tools is possible.
  • portions of the press cake are supplied in frozen form particularly favorable as regrind, so that the oil components can not escape as a liquid.
  • the grinding material fed in takes place in a pin mill that is comparatively insensitive to sticking.
  • the further grinding process may comprise a de-oiling of the feedstock, in particular by extraction, so that the residual oil content in the processed presscake can also be reduced by this measure and its processing is facilitated.
  • the resulting material is the bright color of the cores retains, without being affected by shell parts in its aesthetic effect.
  • Antinutrive components contained in the shell such as waxes or polyphenols, are thus kept away from the food produced.
  • the basic, filling or addition substance obtained forms a powder having particle sizes of approximately from 100 ⁇ to 500 ⁇ .
  • Such a powder can also serve as a raw material for protein extraction (protein concentration and / or protein isolation) because due to the reduction of shell fractions, the crude fiber with antinutriven components is at least largely removed and also in the powder by the oil reduction is a high protein content.
  • the rape proteins contain many important amino acids and can therefore replace animal protein sources. In addition, by grinding - cold or warm - already a digestion has taken place.
  • this powder is well suited as a substitute for soybean in animal feed and even superior to this.
  • rapeseed obtained in the processing and core parts of the rapeseed containing Press cake as a basis for protein extraction and a feed or food to be formed separately claimed.
  • FIG. 3 shows a rough schematic flow diagram of an alternative method according to the invention, in which it is possible to choose between a cryo-milling and a so-called hot-milling at room temperature,
  • FIG. 4 shows a detailed view of different method steps from FIG. 3.
  • These are then introduced into a device S for peeling and thereby into a shell fraction S. G and a nuclear fraction S. E separately.
  • a pressing of the shells is possible;
  • only the pressure P of the cores S .E is shown in Figure 2, which are then further fed to a fine grinding device K.
  • both once PB or multi-milled presscake PD can be subjected to the fine grinding.
  • unpressed cores S .E can be included in the fine grinding.
  • a cryogenic grinding is performed - only by way of example - which operates with frozen ground material, so that the relatively high residual oil content in the material K.B can not lead to smearing or sticking of the machines.
  • FIGS. 3 and 4 it is shown in FIGS. 3 and 4 that a so-called milling process of the mill base W.A can also be carried out at room temperature, dispensing with costly cooling with liquid nitrogen.
  • a fine material KD is obtained which ⁇ a free-flowing powder having particle sizes of from about 100 to 500 ⁇ in approximately a Gauss distribution rule is formed. Due to the use of only cores without shells, the powder KD or WB has a light color. This powder K. D can then be used directly as or at least as a base, filling or addition material for pet food of various kinds.
  • a powder K D or WB thus formed can also serve as a starting material for protein extraction (protein concentration and / or protein isolation), since it has a very high molecular weight Contains protein content with many important amino acids and is free from disturbing raw fibers of the shell. Antinutrive substances such as chlorophyll, tannin, polyphenols, phytic acid are therefore significantly reduced. Such a substance can also very well serve as a substitute for soy a in animal nutrition.
  • the use of meat and / or fish meal in animal feed can be significantly reduced and yet the nutritional content can be increased.
  • the replacement of animal products by the product according to the invention considerably reduces the risk of disease transmission via animal meal (for example BSE), since the product according to the invention contains no pathogenic germs.
  • the requirement of factory farming for the production of animal feed can be reduced.
  • the rape seed is firstly cleaned in the screening machine 1, so that stocking A. c and plow grain A. D can be sorted out and the cleaned rape seed AB dried in a seed drier 2 can, for example in the air stream.
  • the thus cleaned, dried and an approximate standard size rapeseed A. E are then fed to the peeling S, where they are first broken in a double rolling mill 3 in the gap between the rollers;
  • the resulting rapeseed break S .A is fed to a screening machine 4, in the opening S. C and fine break S D be sorted out and the so-called. Nutzbruch SB is further transferred to a classifier 5. In this the shells S.
  • This shelled core fraction S .E is fed to a single- or multi-stage pressing unit P. As shown by way of example in FIG. 2, two screw presses 8, 9 are provided there.
  • a first pressing of the peeled rapeseed S .E is carried out, so that the core oil PA of the first pressing can be obtained.
  • the core cake PB of the first pressing may be subjected to a second pressing in the second press 9 so that the oil yield increases and the core oil increases PC can be obtained additionally.
  • the core cake P.D of the second (or a further) pressing can, like the core cake P.B, be fed to the first pressing and / or unmilled rapeseed kernels S.E as a single fraction or as a mixture of these fractions to the fine grinding K or W as a whole ,
  • the fine grinding K is according to Figures 1 and 2, for example only, a cryogenic, d. H. that the regrind KB after passing through a metal separator 10 in a cooler 1 1, here a vortex screw cooler, frozen, In this cooler 1 1 here liquid nitrogen KA is introduced, so that the still contained in the millbase oil content (typically around 10% for the second and 22% for the first pressing) the grinder is not smeared or glued.
  • the frozen millbase K.C is beaten in a pin mill 12 and thereby converted into the desired fine material K. D of fine grain size in the order of 100 ⁇ up to 500 ⁇ and introduced into a sump 13.
  • the classifying gas K.E is removed from the fine material K.D via a filter 14 and a fan 15.
  • the nitrogen K.F can be used again in a circuit for cooling.
  • the further grinding process need not necessarily comprise a cryogenic grinding process, but may additionally or alternatively in particular include a further de-oiling before the grinding of the feedstock to be fed in, in particular by extraction.
  • FIGS. 3 and 4 also show hot milling W without nitrogen cooling, in which a pin mill 17 is likewise provided for grinding the meal WA and at the end likewise a powder WB is obtained. Due to the fact that only core portions of the rapeseed grains are fed to the further grinding process without the addition of shell portions, the resulting fine grinding material KD, WB also remains light yellowish and without the u. U. For foods unwanted and contained in the cup fractions.
  • the powder K. D, WB can also be processed in various ways, in particular also the foodstuffs formed with the powder, for example also heated or deep-frozen, extruded, in bar or tablet form or otherwise pressed. LIST OF REFERENCE NUMBERS

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Nutrition Science (AREA)
  • Polymers & Plastics (AREA)
  • Mycology (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Proteomics, Peptides & Aminoacids (AREA)
  • Molecular Biology (AREA)
  • Botany (AREA)
  • Seasonings (AREA)
  • Fats And Perfumes (AREA)
  • Fodder In General (AREA)
  • Bakery Products And Manufacturing Methods Therefor (AREA)
  • Edible Oils And Fats (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Meat, Egg Or Seafood Products (AREA)

Abstract

Procédé de traitement de graines de colza (A.A), consistant à les décortiquer et à séparer les parties noyau (S.E) des parties enveloppe (S.G), les parties noyau (S.E) étant soumises à une ou plusieurs pressions pour obtenir de l'huile (P.A; P.C), avec production d'un tourteau (P.B; P.D) à teneur en matières solides et en huile. Selon l'invention, le tourteau (P.B;P.D) est extrait directement ou bien après au moins un autre broyage (K;W) en tant que matière de base, matière de charge ou matière additionnelle (K. D) d'alimentation pour les animaux.
EP10810743A 2009-09-11 2010-09-11 Utilisation de graines de colza décortiquées Withdrawn EP2475268A2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE102009040925A DE102009040925A1 (de) 2009-09-11 2009-09-11 Nutzung von geschälten Rapssamen
CH00276/10A CH701658B1 (de) 2009-09-11 2010-03-02 Nutzung von geschälten Rapssamen.
PCT/EP2010/005576 WO2011029612A2 (fr) 2009-09-11 2010-09-11 Utilisation de graines de colza décortiquées

Publications (1)

Publication Number Publication Date
EP2475268A2 true EP2475268A2 (fr) 2012-07-18

Family

ID=43662318

Family Applications (2)

Application Number Title Priority Date Filing Date
EP10810742.6A Active EP2475267B1 (fr) 2009-09-11 2010-09-11 Utilisation de graines de colza décortiquées
EP10810743A Withdrawn EP2475268A2 (fr) 2009-09-11 2010-09-11 Utilisation de graines de colza décortiquées

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP10810742.6A Active EP2475267B1 (fr) 2009-09-11 2010-09-11 Utilisation de graines de colza décortiquées

Country Status (8)

Country Link
US (2) US9427013B2 (fr)
EP (2) EP2475267B1 (fr)
CA (2) CA2807598A1 (fr)
CH (1) CH701658B1 (fr)
DE (1) DE102009040925A1 (fr)
RU (2) RU2596016C2 (fr)
UA (2) UA105807C2 (fr)
WO (2) WO2011029611A2 (fr)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2783576B1 (fr) 2013-03-29 2017-08-09 AB "Linas Agro Group" Concentré de protéine de colza à partir d'un noyau de colza mécaniquement déshuilé
GB201316196D0 (en) 2013-09-11 2013-10-23 Piksel Inc Triggering an action in a computer device
DE102013110981A1 (de) * 2013-10-02 2015-04-02 Thyssenkrupp Industrial Solutions Ag Verfahren zum Betreiben einer Anlage mit wenigstens einem Aggregat, das eine rotierende Oberfläche aufweist
RU2616794C1 (ru) * 2016-03-21 2017-04-18 Федеральное государственное автономное образовательное учреждение высшего образования "Южно-Уральский государственный университет (национальный исследовательский университет)" (ФГАОУ ВО "ЮУрГУ (НИУ)") Способ приготовления соуса со жмыхом рапса
US20210153522A1 (en) 2017-09-11 2021-05-27 Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung E.V. Method for obtaining protein preparations from sunflower and/or canola oilseeds, and protein preparation
DK3550004T3 (da) 2018-04-03 2020-12-14 Euro Protein Gmbh Fremgangsmåde og indretning til industriel forarbejdning af rapsfrø under udvinding af koldpresset rapskerneolie
CA3136494A1 (fr) 2019-04-09 2020-10-15 Waldemar Neumuller Procede et dispositif de collecte industrielle d'huile de colza et de concentre de proteines de colza a partir de graines de colza
US20230085557A1 (en) * 2020-02-24 2023-03-16 Givaudan Sa Active component delivery systems

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4158656A (en) * 1978-02-27 1979-06-19 Canadian Patents And Development Limited Oilseed processing
EP1074605A1 (fr) * 1999-08-06 2001-02-07 Felix Horst Prof. Dr.-Ing. Schneider Procédé et appareil de production d'huile de cuisson à partir de colza
EP2885980A1 (fr) * 2013-12-19 2015-06-24 Kramerbräu Agro & Food GmbH Procédé et dispositif de fabrication de protéines végétales, en particulier comme aliment ou nourriture riches en protéines, et aliment et nourriture riches en protéines

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US4083836A (en) * 1974-05-17 1978-04-11 Alfa-Laval Ab Production of rapeseed protein concentrate for human consumption
DD127952A5 (de) * 1975-12-02 1977-10-19 Akad Rolniczo Tech Verfahren zur herstellung von eiweisskonzentrat aus rapssamen und anordnung zur durchfuehrung des verfahrens
US4515818A (en) * 1982-03-03 1985-05-07 Csp Foods Ltd. Process for preparing sunflower butter spread from pretreated sunflower seeds
IL145257A0 (en) * 1999-03-17 2002-06-30 Fraunhofer Ges Forschung Method for treating and processing lupine seeds containing alkaloid, oil and protein
US6955831B2 (en) * 2000-05-09 2005-10-18 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Fisheries And Oceans Protein and lipid sources for use in aquafeeds and animal feeds and a process for their preparation
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CA2489505C (fr) * 2002-06-20 2012-04-10 Burcon Nutrascience (Mb) Corp. Reduction de couleur dans un isolat de proteine de canola
LV13176B (en) * 2004-03-15 2004-08-20 Valerijs Finogenovs Use of rapeseed oilcake as additives for bakery products made from flour and/or grain
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Publication number Priority date Publication date Assignee Title
US4158656A (en) * 1978-02-27 1979-06-19 Canadian Patents And Development Limited Oilseed processing
EP1074605A1 (fr) * 1999-08-06 2001-02-07 Felix Horst Prof. Dr.-Ing. Schneider Procédé et appareil de production d'huile de cuisson à partir de colza
EP2885980A1 (fr) * 2013-12-19 2015-06-24 Kramerbräu Agro & Food GmbH Procédé et dispositif de fabrication de protéines végétales, en particulier comme aliment ou nourriture riches en protéines, et aliment et nourriture riches en protéines

Non-Patent Citations (1)

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See also references of WO2011029612A2 *

Also Published As

Publication number Publication date
EP2475267B1 (fr) 2019-06-19
RU2012114131A (ru) 2013-11-10
WO2011029611A3 (fr) 2011-06-03
WO2011029612A3 (fr) 2011-05-26
CA2807596C (fr) 2019-05-07
US20120276276A1 (en) 2012-11-01
CH701658A2 (de) 2011-03-15
UA106893C2 (uk) 2014-10-27
US9642388B2 (en) 2017-05-09
WO2011029612A2 (fr) 2011-03-17
UA105807C2 (uk) 2014-06-25
RU2596016C2 (ru) 2016-08-27
WO2011029611A2 (fr) 2011-03-17
US20130001333A1 (en) 2013-01-03
CA2807596A1 (fr) 2011-03-17
EP2475267A2 (fr) 2012-07-18
CA2807598A1 (fr) 2011-03-17
CH701658B1 (de) 2011-06-30
DE102009040925A1 (de) 2011-03-31
RU2596039C2 (ru) 2016-08-27
US9427013B2 (en) 2016-08-30
RU2012114129A (ru) 2013-10-27

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