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WO2014111151A1 - Aliments ou granulés pour animaux, contenant des matières grasses - Google Patents

Aliments ou granulés pour animaux, contenant des matières grasses Download PDF

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Publication number
WO2014111151A1
WO2014111151A1 PCT/EP2013/050917 EP2013050917W WO2014111151A1 WO 2014111151 A1 WO2014111151 A1 WO 2014111151A1 EP 2013050917 W EP2013050917 W EP 2013050917W WO 2014111151 A1 WO2014111151 A1 WO 2014111151A1
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WO
WIPO (PCT)
Prior art keywords
pellets
mass
food
weight
water
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.)
Ceased
Application number
PCT/EP2013/050917
Other languages
German (de)
English (en)
Inventor
Konrad Munz
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.)
Buehler AG
Original Assignee
Buehler AG
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 Buehler AG filed Critical Buehler AG
Priority to PCT/EP2013/050917 priority Critical patent/WO2014111151A1/fr
Publication of WO2014111151A1 publication Critical patent/WO2014111151A1/fr
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K40/00—Shaping or working-up of animal feeding-stuffs
    • A23K40/20—Shaping or working-up of animal feeding-stuffs by moulding, e.g. making cakes or briquettes
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K10/00—Animal feeding-stuffs
    • A23K10/30—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K40/00—Shaping or working-up of animal feeding-stuffs
    • A23K40/25—Shaping or working-up of animal feeding-stuffs by extrusion
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/40—Feeding-stuffs specially adapted for particular animals for carnivorous animals, e.g. cats or dogs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/40—Feeding-stuffs specially adapted for particular animals for carnivorous animals, e.g. cats or dogs
    • A23K50/42—Dry feed
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K50/00—Feeding-stuffs specially adapted for particular animals
    • A23K50/80—Feeding-stuffs specially adapted for particular animals for aquatic animals, e.g. fish, crustaceans or molluscs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L11/00—Pulses, i.e. fruits of leguminous plants, for production of food; Products from legumes; Preparation or treatment thereof
    • A23L11/01—Pulses or legumes in the form of whole pieces or fragments thereof, without mashing or comminuting
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
    • A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/20—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
    • A23L29/206—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin
    • A23L29/212—Starch; Modified starch; Starch derivatives, e.g. esters or ethers
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P30/00—Shaping or working of foodstuffs characterised by the process or apparatus
    • A23P30/20—Extruding

Definitions

  • the present invention relates to methods of preparing fatty food or feed pellets, food or feed pellets per se, pellet containing compositions and uses of pellets.
  • Food and feed pellets can contain a variety of in ⁇ halt materials such as fats, starch and proteins. Physiologically particularly valuable are fats containing omega-3 fatty acids. There is thus a need for pellets with the highest possible proportion of such fatty acids. Such fatty acids are contained in oilseeds. For example, flaxseed is about 50% by weight of fat, with 70% by weight of it being omega-3 fatty acids.
  • a method for producing fatty food or feed pellets, wel ⁇ ches containing the following steps: a) providing or producing a mass containing a solids content and water, wherein the solids content of at least one fatty component , in particular Minim ⁇ least includes an oil seed, and the total proportion of fetthal ⁇ term component (s) in the solids content in the range of 1 wt .-% to 99 wt .-%, preferably of 25 wt .-% to 95 wt .-% , more preferably from 50 wt .-% to 85 wt .-%, particularly preferably ⁇ from 60 wt .-% to 80 wt .-%; b) cooking the mass; c) removing at least part of the water contained in the mass; d) shaping the mass into pellets.
  • the fatty component is preferably ei ⁇ ne oilseed.
  • at least one of the fat-containing components but, for example, fish meal or meat meal may be.
  • the fat-containing component may have a fat content in the range of 5 to 60% by weight.
  • the fat content of linseed may range from 47 to 57% by weight; the fat content of meat meal may range from 7 to 23% by weight.
  • the maximum proportion of fat-containing component (s) in the mass is limited by its fat content and the binding property of an optional starch-containing substance described in more detail below.
  • proportions by weight of the fat-containing component (s) in the solids content of up to 95 or even 99% by weight, without the pellets becoming mechanically unstable.
  • the solids content of the composition provided or prepared in step a) may contain, in addition to the fatty component (s), at least one starch-containing substance.
  • These starch-containing substance ⁇ can lead by cooking in step b) to a sufficient plasticizing binding of the pellets.
  • the starch-containing substance may be, for example, a cereal or a legume.
  • the grain can Wei ⁇ zen, corn, barley, oats, rye, barley, millet, rice or any mixture thereof may or consist thereof.
  • the legume may be, for example, peas (pisum sativum) or field beans.
  • the starchy substance can also be potatoes or manioc.
  • the cereal and / or legume may be used in the form of flour or meal.
  • Legumes such as Erb ⁇ sen, or cereals, potatoes or cassava can be present as pure starch.
  • the amount of starch in the solids content may range from 1% to 80%, preferably from 5% to 60%, more preferably from 10% to 40%, by weight preferably from 10 wt .-% to 15 wt .-% starch, based on the solids content. As tests have shown, a proportion of 10% by weight or even only 1% by weight of starch in the solids content is sufficient for sufficient plasticization and thus for sufficient stability of the pellets.
  • a starch content of 10 to 15 wt .-% in the solids content can be achieved, which still leads to mecha ⁇ nisch stable pellets.
  • a weight proportion of 95% by weight of the fat-containing component is possible, for example, if the fat-containing component is meat-and-bone flour and the remaining 5% by weight of the solids content is pea starch.
  • the solids content contains 90% by weight of flaxseed and 10% by weight of erb ⁇ senair or 75 wt .-% linseed and 25 wt .-% peas.
  • the total amount of starch in the composition prepared or provided in step a) may range from 1% to 80%, preferably from 5% to 80%, more preferably 10%, by weight. -% to 50 wt .-%, particularly preferably from 12 wt .-% to 30 wt .-% are.
  • the temperature of the mass in the cooking in step b) may be at least 100 ° C and is preferably in the range of 100 ° C to 140 ° C, more preferably from 110 ° C to 130 ° C. With such high temperatures sufficient plasticization and thus mechanically stable pellets can be achieved.
  • the at least partial removal of the water in step c) can take place, for example, by at least partial evaporation and / or evaporation of the water.
  • the Verduns ⁇ tion and / or evaporation can be effected by means of a negative pressure or reinforced.
  • the negative pressure can be achieved for example with a vacuum pump. Is also a part of the ent ⁇ fernten water vapor may be recycled into the preconditioner, as for example, in WO 97/14312 explained.
  • step c) 1 wt .-% to 8 wt .-%, more preferably 1 wt .-% to 5 wt .-%, particularly preferably 1 wt .-% to 4 wt .-% of the contained in the mass Water removed.
  • This proportion can be adjusted by means of a pressure adjusting agent, as described in WO 2006/092070.
  • This pressure setting means may be a retaining work with include the Extru ⁇ the return conveying screw. This can be prevented that together with the removed water and a part of the mass exits. In this way the pressure prevailing in the mass vapor pressure can be regulated, whereby the degree of expansion of the pellets after molding in step d) affects who can ⁇ .
  • the mass flow between steps b) and c) can be regulated by means of an adjustable barrier.
  • an adjustable barrier as described, for example, in WO 2006/092070, the specific mechanical energy introduced during the process can be adjusted by inhibiting the delivery of the compound. In addition, this also allows the temperature in step b) to be set.
  • the temperature of the mass decreases due to the removal of the water.
  • the temperature ⁇ structure of the mass in step d) in the range from 80 ° C to 110 ° C, be ⁇ vorzugt of 90 ° C to 105 ° C and particularly preferably min ⁇ least 90 ° C but less than 100 ° C be. Temperatures less than or equal to 100 ° C may prevent undesirable expansion of the pellets. At higher temperatures, the vapor pressure ⁇ ren would inflate the parison and weaken the structure, which would result in a lower mechanical bond at high fat and low starch content.
  • At least the steps b) to d) can be carried out in a Zweiwellenex ⁇ truder.
  • a twin-screw extruder has the advantage over a single-screw extruder used in the known methods that, despite its high fat content, the compound can be conveyed and processed largely independently of the wall friction by the process.
  • a co-rotating twin-screw extruder is particularly suitable, which also also provides for a self-cleaning effect.
  • the forming in step d) can extruder by means of at least one nozzle of two-shaft ⁇ .
  • Step a) may include conditioning in which at least a portion of the solids content, especially at least one fatty component such as an oilseed, is added to water and / or steam.
  • the resulting mass can already be preheated.
  • the conditioning is carried out for a period of time which is in the range from 5 s to 200 s, more preferably from 20 s to 120 s and particularly preferably from 20 s to 60 s ,
  • flaxseed contains such enzymes to protect against attack by insects.
  • a milling can for example be accomplished with the aid of at least a hammer mill and / or at least a hammer mill and / or at least one rolling mill , wherein the Vermah ⁇ ment is carried out in particular prior to conditioning.
  • the pellets can be dried to make them durable for subsequent storage and transportation.
  • the pellets may still be at such a high temperature that they are fragile.
  • the pellets should be possible scho ⁇ Nend be fed to the drying. For example, if they fall from an extrusion die into a dryer solely due to their gravity, then the drop height should be kept as low as possible.
  • the pellets are to be transported pneumatically after extrusion, they should be previously cooled, for example to temperatures in the range of 20 ° C to 60 ° C. In this temperature range, the pellets are then sufficiently stable.
  • oilseed may be, for example, flaxseed, soy, rapeseed or sunflower. Corn germ and rice bran can also be inactivated and encapsulated in this way.
  • the invention further relates to food or feed pellets which are he ⁇ biblich by a process as described above.
  • These pellets differ from known, containing a fatty component pellets by the height ⁇ ren proportion of the fat-containing component and / or by their higher mechanical stability.
  • the proportion of the fat-containing component (s), in particular in the case of linseed in the range of 1 wt .-% to 99 wt .-%, preferably from 25 wt .-% to 90 wt .-%, more preferably from 50% by weight to 85% by weight, more preferably from 60 wt .-% to 80 wt .-%, based on the total weight of the pellets.
  • This proportion depends on the fat content of the fatty components and the starch content of the starchy substance.
  • the fat content can be determined by conventional methods, for example by the Soxhlet method.
  • compositions containing food or feed pellets as described above may be, for example, a fish food composition, a pet food composition, a feed composition or a food composition.
  • the invention also relates to the use of food or feed pellets, which were produced with a method as described above ⁇ NEN, or a composition as described above as fish feed, petfood, as feed or as food.
  • a partial encapsulation of the fats can be achieved, which reduces their oxidation.
  • a homogeneous mixture of starch and fat achieves a matrix that reduces the exchange of atmospheric oxygen with the labile components of the fat.
  • FIG. 1 shows a first system for carrying out a method according to the invention
  • FIG. 1 shows a first installation 10, which is designed to carry out the method according to the invention.
  • the installation 10 ent ⁇ holds three dosage units 11, 14, 17, which up to three different in each case via a funnel 12, 15, 18 and a screw conveyor 13, 16, 19 Availability checked ⁇ gene.
  • Using these metering devices 11, 14, 17 may Solids are introduced through a metering tube 20 into a preconditioner 21. At least one of the solids is a fatty component, namely be ⁇ vorzugt an oilseed, such as linseed, rape, sun flowers ⁇ or soy.
  • the solids so do ⁇ Siert that the proportion by weight of the fatty component, the ⁇ particular of the oil seed, based on the total solids content in the range of 1 wt .-% to 99 wt .-%, preferably of 25 wt .-% to 95 wt .-%, preferably from 50 wt .-% to 85 wt .-%, particularly preferably from 60 wt .-% to 80 wt .-% is.
  • the oil seed provided in one or more of the funnels 12, 15 or 18 has an average particle size of less than 1 mm.
  • a particularly effective inactivation of any digestive substances or enzymes can be achieved.
  • Such a medium Pellegrös ⁇ se can be achieved, for example, that the oil seed is previously ground in a grinding unit, not shown here, for example in a hammer mill, a hammer mill o- of a rolling mill.
  • the cereals may, for example, be wheat, corn, vegetables , rye, barley, millet, oats or rice.
  • the legume may be, for example, peas (pisum sativum) or field beans.
  • the starchy substance can also be potatoes or manioc.
  • the cereals and / or legume may, for example, be be supplied in the form of flour or meal. Legumes such as peas, or cereals, potatoes or manioc can be fed as pure starch.
  • the amount of starch based on the total solids content can be in the range from 1% by weight to 80% by weight, preferably from 5% by weight to 60% by weight, more preferably from 10% by weight to 40% by weight. %, more preferably from 10 wt .-% to 15 wt .-% are.
  • the solids metered in by the metering tube 20 are supplied with water through a water feed line 22 and steam through a steam feed line 23.
  • the Wasserzulei ⁇ tung 22 includes a shutoff valve 24 and a flow meter 25.
  • the steam supply 23 also has a valve 26.
  • the preconditioner 21 may, for example, be the model BCTC, which is available from Buhler AG, 9240 Uzwil, Switzerland , It has been shown that a suffi ⁇ sponding conditioning can be reached in less than one minute.
  • the mass After leaving the preconditioner 21, the mass has a Tem ⁇ temperature of about 95 ° C.
  • a line 27 it is fed to a StopfSchneckentician 28 which they ein approvalt in a ⁇ A enters zone 32 of a corotating twin-screw extruder 30 toward ⁇ .
  • a twin-screw extruder 30 for example, the BCTG model from Bühler AG can be used.
  • a supply line 29 of the mass during the passage of the StopfSchneckentician 28 further water can be supplied.
  • the two shafts, not shown here, of the twin-screw extruder 30 are driven by means of a motor 31.
  • the mass In the entry zone 32, the mass has a temperature of 95 ° C. It is subsequently heated to a temperature in the range from 110 ° C. to 130 ° C. The heating takes place on the one hand due to the energy input, which is caused by the extruder shafts, as well as due to an additional, not shown here Heater. The temperatures mentioned lead to a boiling of the mass.
  • there is a plasticization of the starch contained in the mass which is sufficient to produce mechanically stable pellets.
  • a fourth extruder section 34 includes a degassing port 35 through which at least a portion of the water contained in the mass can be removed by evaporation.
  • the degassing pipe 35 may have a retaining mechanism with screws, not shown here, in order to prevent that together with the withdrawn steam and the mass itself exits from the two-shaft ⁇ nextruder 30.
  • the degassing pipe 35 is connected to a steam supply pipe 36, a first steam exhaust pipe 37 and a second steam exhaust pipe 38. By opening one of the valves 39, 40 of the mass of water vapor can be withdrawn. This water vapor can then be fed through the first steam discharge line 37 to a solids separator 41.
  • Condensed liquid can be supplied to a drain 43.
  • a feed line 44 further water can be added to the solids separator 41.
  • the water vapor is separated together with a small amount of dust and aroma components and fed by means of a metering pump 45 as a warm, low solids laden water through a flow meter 46 and a line 47 again the preconditioner 21.
  • an adjustable barrier can be provided, as described for example in WO 2006/092070. With such an adjustable barrier, the specific mechanical energy in the cooking zone and so that the prevailing temperature of the mass adjusted ⁇ who.
  • the temperature of the mass falls within a range of 90 ° C to 105 ° C.
  • the mass can then be formed into pellets. Through a drop tube 49, the pellets at a temperature of about 90 ° C to
  • pellets should not be sufficiently mechanically stable in the temperature range ge ⁇ called the drop height between mold unit should be minimized corresponding to 48 and dryer 50th
  • FIG. 2 shows a slightly modified second system 10 '.
  • this system 10 reach the exit from the mold unit 48 ⁇ the pellets initially in a cooling device 51, in which they can be cooled to a temperature ranging from 20 ° C to 60 ° C.
  • the pellets can be sorted by hand ⁇ their quality: Either you are directed into a reject bin 53 or fed to a pneumatic conveyor unit 54th
  • additives may also be added to the composition, for example in the preconditioner 21 or in the twin- screw extruder 30.
  • additional additives may be, for example, salts, oils, vitamins, antioxidants or other stabilizers which are used in the production of foods, feedstuffs, etc . are suitable.
  • pellets with the following formulations were produced with the above-described systems 10, 10 ':
  • Example 1 Example 1 :
  • the fat content in this recipe is about 29 wt .-%, the starch content about 18 wt .-%. From this recipe, cuboidal pellets having dimensions of 15 mm ⁇ 22 mm ⁇ 6 mm for use as horse feed were produced by the method according to the invention. Extrusion was possible without any problems.
  • the fat content in this formulation is about 14% by weight, the starch content about 25% by weight.
  • the fat content in this recipe is about 36 wt .-%, the starch content about 11 wt .-%.
  • the fat content on dry basis is about 36% and the starch content is about 11%. If the proportion of flaxseed increases the mechanical stability of Pel ⁇ lets reduced.

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Zoology (AREA)
  • Animal Husbandry (AREA)
  • Birds (AREA)
  • Health & Medical Sciences (AREA)
  • Botany (AREA)
  • Nutrition Science (AREA)
  • Dispersion Chemistry (AREA)
  • Biotechnology (AREA)
  • Manufacturing & Machinery (AREA)
  • Molecular Biology (AREA)
  • Mycology (AREA)
  • Physiology (AREA)
  • Agronomy & Crop Science (AREA)
  • Insects & Arthropods (AREA)
  • Marine Sciences & Fisheries (AREA)
  • Fodder In General (AREA)

Abstract

La présente invention concerne d'une part un procédé pour fabriquer des aliments ou des granulés pour animaux, contenant des matières grasses, ledit procédé comprenant les étapes suivantes : a) fournir ou fabriquer une masse renfermant une certaine teneur en solides ainsi que de l'eau, la teneur en solides contenant au moins un composant gras, en particulier au moins un oléagineux et la proportion totale de composant(s) gras dans la teneur en matières grasses se situe dans la plage de 1 % à 99 % en poids, de préférence de 25 % à 95 % en poids, de préférence encore de 50 % à 85 % en poids, de manière particulièrement préférée de 60 % à 80 % en poids; b) cuire la masse; c) éliminer au moins une partie de l'eau contenue dans la masse; d) façonner la masse sous forme de granulés. D'autres aspects de l'invention concernent des granulés fabriqués avec ce procédé, les compositions comportant ce type de granulés ainsi que des utilisations de ces granulés ou compositions.
PCT/EP2013/050917 2013-01-18 2013-01-18 Aliments ou granulés pour animaux, contenant des matières grasses Ceased WO2014111151A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/EP2013/050917 WO2014111151A1 (fr) 2013-01-18 2013-01-18 Aliments ou granulés pour animaux, contenant des matières grasses

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/EP2013/050917 WO2014111151A1 (fr) 2013-01-18 2013-01-18 Aliments ou granulés pour animaux, contenant des matières grasses

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104397858A (zh) * 2014-11-14 2015-03-11 无锡乐华自动化科技有限公司 一种秸秆饲料自动化加工装置及秸秆饲料制备方法
US10244777B2 (en) 2015-05-16 2019-04-02 Big Heart Pet, Inc. Palatable expanded food products and methods of manufacture thereof
CN113974020A (zh) * 2021-09-15 2022-01-28 福建天马科技集团股份有限公司 一种卵形鲳鲹专用配合饲料，及其生产用设备
WO2023214058A1 (fr) * 2022-05-06 2023-11-09 Planted Foods Ag Appareil de traitement d'articles alimentaires protéiques à base de plantes, ensemble d'articles alimentaires et procédé de traitement

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0041641A2 (fr) * 1980-06-10 1981-12-16 Textruder Engineering Ag Procédé et extrudeuse à double vis pour la transformation de subtances en poudre ou en farine et sèches, en aliments sous une forme digestible
DE4042354A1 (de) * 1990-09-21 1992-03-26 Allkraft Futtermittel Gmbh Futtermittel aus leinsamen
GB2269084A (en) * 1992-07-29 1994-02-02 Buxted Chicken Limited Animal feeds
FR2768025A1 (fr) * 1997-09-05 1999-03-12 Unicopa Supplement energetique a l'alimentation des vaches laitieres et son procede de fabrication
CA2319978A1 (fr) * 2000-09-20 2002-03-20 Westcan Alfalfa Inc. Methode de production d'aliments agglomeres pour les animaux
WO2006063444A1 (fr) * 2004-12-15 2006-06-22 O & T Farms Preparation et utilisation d'aliments pour animaux a haute teneur en omega-3 et omega-6
WO2010040884A1 (fr) * 2008-10-06 2010-04-15 Consejo Superior De Investigaciones Científicas (Csic) Composition pour complément alimentaire

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0041641A2 (fr) * 1980-06-10 1981-12-16 Textruder Engineering Ag Procédé et extrudeuse à double vis pour la transformation de subtances en poudre ou en farine et sèches, en aliments sous une forme digestible
DE4042354A1 (de) * 1990-09-21 1992-03-26 Allkraft Futtermittel Gmbh Futtermittel aus leinsamen
GB2269084A (en) * 1992-07-29 1994-02-02 Buxted Chicken Limited Animal feeds
FR2768025A1 (fr) * 1997-09-05 1999-03-12 Unicopa Supplement energetique a l'alimentation des vaches laitieres et son procede de fabrication
CA2319978A1 (fr) * 2000-09-20 2002-03-20 Westcan Alfalfa Inc. Methode de production d'aliments agglomeres pour les animaux
WO2006063444A1 (fr) * 2004-12-15 2006-06-22 O & T Farms Preparation et utilisation d'aliments pour animaux a haute teneur en omega-3 et omega-6
WO2010040884A1 (fr) * 2008-10-06 2010-04-15 Consejo Superior De Investigaciones Científicas (Csic) Composition pour complément alimentaire

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
OLAV FJELD KRAUGERUD ET AL: "Physical properties of extruded fish feed with inclusion of different plant (legumes, oilseeds, or cereals) meals", ANIMAL FEED SCIENCE AND TECHNOLOGY, ELSEVIER, AMSTERDAM, NL, vol. 163, no. 2, 24 November 2010 (2010-11-24), pages 244 - 254, XP028128457, ISSN: 0377-8401, [retrieved on 20101130], DOI: 10.1016/J.ANIFEEDSCI.2010.11.010 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104397858A (zh) * 2014-11-14 2015-03-11 无锡乐华自动化科技有限公司 一种秸秆饲料自动化加工装置及秸秆饲料制备方法
US10244777B2 (en) 2015-05-16 2019-04-02 Big Heart Pet, Inc. Palatable expanded food products and methods of manufacture thereof
US11297853B2 (en) 2015-05-16 2022-04-12 Big Heart Pet, Inc. Palatable expanded food products and methods of manufacture thereof
CN113974020A (zh) * 2021-09-15 2022-01-28 福建天马科技集团股份有限公司 一种卵形鲳鲹专用配合饲料，及其生产用设备
CN113974020B (zh) * 2021-09-15 2024-03-26 福建天马科技集团股份有限公司 一种卵形鲳鲹专用配合饲料，及其生产用设备
WO2023214058A1 (fr) * 2022-05-06 2023-11-09 Planted Foods Ag Appareil de traitement d'articles alimentaires protéiques à base de plantes, ensemble d'articles alimentaires et procédé de traitement

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