EP0915664A1 - Procede pour incorporer des matieres grasses dans un produit granule - Google Patents
Procede pour incorporer des matieres grasses dans un produit granuleInfo
- Publication number
- EP0915664A1 EP0915664A1 EP96922726A EP96922726A EP0915664A1 EP 0915664 A1 EP0915664 A1 EP 0915664A1 EP 96922726 A EP96922726 A EP 96922726A EP 96922726 A EP96922726 A EP 96922726A EP 0915664 A1 EP0915664 A1 EP 0915664A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- mixer
- product
- liquid
- fat
- granules
- 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- Withdrawn
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
-
- 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
- A23K40/30—Shaping or working-up of animal feeding-stuffs by encapsulating; by coating
-
- 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
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P20/00—Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
- A23P20/10—Coating with edible coatings, e.g. with oils or fats
- A23P20/11—Coating with compositions containing a majority of oils, fats, mono/diglycerides, fatty acids, mineral oils, waxes or paraffins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S426/00—Food or edible material: processes, compositions, and products
- Y10S426/805—Pet food for dog, cat, bird, or fish
Definitions
- a product is greased together with a greasing liquid in such a way that the greasing liquid not only remains on the surface, but penetrates into the interior
- the greasing is carried out after the shaping process by means of spray drums or mixers in a conventional manner, there is the problem that the product to be greased only absorbs the greasing liquid on the surface, or that the greasing liquid penetrates the product only slowly by means of the capillary action, which is slowed down with increasing viscosity or closed or small pores
- the amount of fat that can be applied to the product by means of spray drums or mixers is limited to 5 to 10% of the amount of granules
- One improvement in this regard is shown and described in Japanese patent application with publication number HEI3-180 163 (1991), in which a product is brought into an obliquely upward-facing auger by means of a metering lock, an oil sump with a predetermined value being placed in a lower part of the inclined auger The level at which the product falls and is moistened when it is transported upwards is maintained.
- the screw is additionally depressurized by means of a vacuum pump, ie the product which is required after the greasing liquid is in a predetermined vacuum during transport
- the level of the so-called oil sump can be adjusted and varied
- the oil absorption improves from the aforementioned 5 to 10% of the amount of granules in the conventional method up to 13.5% of the amount of granules in the aforementioned system
- Fish feed recipes which usually contain a large proportion of fish meal, are extruded gently, for example in extruders, at temperatures around 120 ° C with a water content of 20 to 30%.
- this plastic material in the extruder expands at temperatures above 100 ° C associated vapor pressure to solidify as a bread-like, foamy structure when it emerges from the extruder and thus when the moisture escapes and the associated cooling
- such a dried product is placed in a mixer, preferably in a paddle mixer, which stands on weighing cells, so that, based on the measured product weight, the predetermined amount of greasing liquid can be added.
- This predetermined amount of greasing liquid is metered in while rotating the mixer to the Wetting the surfaces of the product parts
- the mixer is placed under negative pressure, as a result of which the air is evacuated from the capillaries of the product
- the product parts have a predetermined temperature, which corresponds to a low viscosity of the greasing liquid, in order to be able to penetrate well into the capillaries or pores of the product during the step, according to the invention, explained later.
- This step according to the method consists in that after the generation of the vacuum, while simultaneously greasing the product, the vacuum in the mixer, and thus the surroundings of the product, is relaxed, so that the atmospheric air that is now entering the mixer again, the greasing air on the surface of the product Liquid in the evacuated pores or capillaries
- the greasing liquid is added below 10%, which is also advantageously carried out according to the invention and in the case of very porous product parts, the greasing liquid is advantageously sprayed in the mixer in order to achieve a uniform wetting of the surface
- spraying can be dispensed with, i.e. the liquid to be greased can be absorbed by the product, i.e. by the product parts during the mixing process, partly from the bottom of the mixer
- the greased product or the greased product parts are advantageously fed to a cooler or a ventilated storage cell at a temperature of approximately 40 ° C.
- the advantage of the method according to the invention, on the one hand - as already mentioned above - is that significantly more fat content per amount of granules is bound to the product than according to the prior art method in which only the wetted product is subjected to a vacuum without Mixing a relaxation of the vacuum takes place, in which the greasing liquid can be absorbed more in the pores or capillaries
- the figure shows a system according to the invention with the device according to the invention, shown schematically
- the figure shows schematically a plant for the production of extrudates and the greasing of these extrudates according to the invention.
- the invention is not restricted to the use in such a plant, but can be used in all plants which produce other porous product parts, such as pellets, expander pellets etc.
- the floury or granular product is known to be moisture-moist for the treatment in the subsequent extruder or expander , prepared for temperature and consistency
- extruder or expander is a machine known per se, for example a twin-shaft extruder of the BI-EX brand, manufactured and sold by the applicant, or an expander, for example with the designation DFEA 220 or a cube press with the designation "KUBEX” , also manufactured and sold by the applicant
- the extruded or expanded product is placed in a dryer, for example a belt dryer, also manufactured and sold by the applicant, in which the extrudates or expandates are dried and cooled
- the exhaust air from the dryer 5 is collected by means of an exhaust hood 6 and fed to a cyclone 7.
- the clean air is discharged as exhaust air 8 into the atmosphere or into another filter (not shown).
- the separated solid substance of the cyclone 7 is collected in a collecting container 9
- the product dried in the dryer 5 is placed in an intermediate container 10, which as a rule has approximately the volume of the subsequent mixer 12, in order thereby to give the mixer 12 the possibility of working in batches. run of the intermediate container 10, a slide 11 is provided, which allows the contents of the intermediate container 10 to pass through the subsequent mixer 12
- the mixer 12 stands on weighing cells 13, so that a predetermined amount can be added to the mixer 12, on the one hand to let the slide 1 close when the amount has been reached and on the other hand to have the corresponding amount of greasy liquid added, for which purpose the product quantity measured by the weighing cells in Mixer of a controller 19 is signa ert
- the controller 19 closes the slide 11 for a predetermined amount in the mixer and, on the basis of the pressure weight signaled by the weighing cells 13, calculates the predetermined, correct amount of greasing liquid which, by means of a metering pump 18, flows from a container 17 for the greasing liquid into the mixer 12 is pumped
- a control satellite 19 1 of the controller 19 puts a vacuum pump 20 into operation after a predetermined time, in order to mix the mixer and.
- This negative pressure evacuates the pores or capillaries of the individual product parts, which manifests itself in the product, for example, in that the air emerging from the pores or capillaries generates foam bubbles in the moisture lying on the surface of the individual product parts
- control satellite 19 1 controls a relief valve 21, to which is connected between the mixer 12 and the vacuum pump 20 on the connecting line from the mixer 12 to the vacuum pump 20
- the mixer is added as a percentage of greasing liquid as experience has shown that the product to be greased is able to absorb, so that when the mixer 12 is emptied, no greasy liquid that has not been absorbed remains at the bottom of the mixer
- the expansion valve can be provided as a pressure control valve, so that the air that flows back in flows back in a controlled manner
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Polymers & Plastics (AREA)
- Food Science & Technology (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Birds (AREA)
- Animal Husbandry (AREA)
- Marine Sciences & Fisheries (AREA)
- Insects & Arthropods (AREA)
- Fodder In General (AREA)
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
- Edible Oils And Fats (AREA)
- Formation And Processing Of Food Products (AREA)
Abstract
L'invention concerne un procédé et un dispositif pour incorporer des matières grasses dans des produits alimentaires granulés pour animaux, par ex. des extrudats, des pastilles, des pastilles expansées etc., avec un liquide fournisseur de graisse. Les pastilles produites dans l'extrudeuse ou dans la zone d'expansion de la presse (4) sont séchées dans une unité de séchage (5) puis passent par un contenant intermédiaire (10) avant d'arriver à un mélangeur (12). Au moyen d'une pompe de dosage (18), une quantité prédéterminée de liquide fournisseur de graisse est incorporée dans le mélangeur (12) et répartie à la surface des particules de produit lors du processus de mélange. Après une période prédéterminée, une pompe à vide (20) produit une dépression dans le mélangeur de façon à évacuer l'air se trouvant dans les capillaires ou les pores des particules de produit. La dépression dans le mélangeur (12) est ensuite supprimée par une soupape de détente (21) de sorte que l'air pénétrant dans le mélangeur et dans les pores ou les capillaires des particules de produit transporte le liquide fournisseur de graisse se trouvant à la surface des particules ainsi que du liquide fournisseur de graisse supplémentaire dans les pores ou les capillaires jusqu'à ce que ces derniers soient remplis de façon à ce qu'une proportion élevée d'environ 30 % de liquide fournisseur de graisse soit liée dans les pores ou les capillaires des particules de produit. Une fois ce processus achevé, le produit est introduit dans un contenant intermédiaire (14) d'où il est distribué en tant que produit final au moyen d'un élément de distribution et de dosage.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/CH1996/000265 WO1998003080A1 (fr) | 1996-07-23 | 1996-07-23 | Procede et dispositif pour incorporer des matieres grasses dans un produit granule |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0915664A1 true EP0915664A1 (fr) | 1999-05-19 |
Family
ID=4550441
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96922726A Withdrawn EP0915664A1 (fr) | 1996-07-23 | 1996-07-23 | Procede pour incorporer des matieres grasses dans un produit granule |
Country Status (4)
Country | Link |
---|---|
US (1) | US6136353A (fr) |
EP (1) | EP0915664A1 (fr) |
JP (1) | JP3985906B2 (fr) |
WO (1) | WO1998003080A1 (fr) |
Families Citing this family (31)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AU3107297A (en) * | 1996-06-14 | 1998-01-07 | Meija Seika Kaisha Ltd. | Process for the production of composite fatty confectionery |
CA2263534A1 (fr) * | 1996-09-05 | 1998-03-12 | Nisshin Flour Milling Co., Ltd. | Procede d'adjonction de matieres grasses a du fourrage poreux |
DE19856680C1 (de) | 1998-12-09 | 2000-08-17 | Effem Gmbh | Verfahren zum Vakuumbeschichten eines extrudierten Nahrungsmittels |
NO309253B1 (no) * | 1999-03-25 | 2001-01-08 | Nutreco Aquaculture Res Ct As | Fremgangsmåte ved fremstilling av fôrpelleter og anlegg for bruk ved gjennomföring av fremgangsmåten |
DE19962866A1 (de) * | 1999-12-24 | 2001-07-05 | Effem Gmbh | Verfahren zum Herstellen gefüllter Nahrungsmittel-Hohlkörper |
CN100502644C (zh) * | 2000-01-20 | 2009-06-24 | 马泰克生物科学公司 | 饲养兔子的方法 |
DE10029079B4 (de) * | 2000-06-13 | 2006-04-20 | Mars Inc. | Probiotische Mikroorganismen enthaltendes Nahrungsmittelerzeugnis |
NO313222B1 (no) * | 2000-09-22 | 2002-09-02 | Nutreco Aquaculture Res Ct As | Fremgangsmåte ved fremstilling av fôrpellet og anlegg for bruk ved fremgangsmåtens gjennomföring |
NO316013B1 (no) * | 2000-10-03 | 2003-12-01 | Tto Seafarm Products As | Fremgangsmåte og apparat til behandling av fiskefôr |
NL1018308C2 (nl) * | 2001-06-15 | 2002-12-17 | Bvba Europ Business Support N | Vet bevattende melkvervanger voor jongvee, werkwijze voor de bereiding van de vet bevattende melkvervanger en de daarbij toe te passen inrichting. |
US7585533B2 (en) * | 2002-06-11 | 2009-09-08 | Nestec S.A. | Pressure formed pet food and method |
US20040096546A1 (en) * | 2002-11-14 | 2004-05-20 | Gillessen Hubert Jean-Marie Francois | Fat-containing milk substitute for young stock, method for preparing the fat-containing milk substitute and device to be used therewith |
NO319624B1 (no) | 2003-09-15 | 2005-09-05 | Trouw Internat Bv | Fiskefôr for laksefisk i ferskvann og anvendelse av slikt fôr. |
NO323529B1 (no) * | 2004-05-13 | 2007-06-04 | Trouw Internat Bv | Framgangsmate for reduksjon av innholdet av uonskede naeringsstoffer i avlopsvann fra fiskeoppdrettsanlegg. |
RU2007137003A (ru) * | 2005-03-08 | 2009-04-20 | Нестек С.А. (Ch) | Способ изготовления питательных композиций |
NO322697B1 (no) | 2005-03-18 | 2006-11-27 | Fishfeed As | Fremgangsmate for fremstilling av fiskefôr med hoyt innhold av vann og lipid. |
BRPI0601166B1 (pt) * | 2006-03-31 | 2016-04-05 | Intecnial S A | equipamento para inativação de grãos. |
EP2173856A1 (fr) * | 2007-06-28 | 2010-04-14 | Chr. Hansen A/S | Traitement de suspension de cellules |
US9771199B2 (en) | 2008-07-07 | 2017-09-26 | Mars, Incorporated | Probiotic supplement, process for making, and packaging |
US20120076895A1 (en) * | 2009-04-23 | 2012-03-29 | Bacterfield Ou | Extruded food products comprising probiotic micro-organisms |
US20110104327A1 (en) * | 2009-04-23 | 2011-05-05 | Bacterfield International S.A. | Probiotic pet food |
CA2765887C (fr) | 2009-06-24 | 2018-08-07 | Land O'lakes Purina Feed Llc | Particules d'alimentation a teneur elevee en matiere grasse |
GB0920596D0 (en) * | 2009-11-24 | 2010-01-06 | Seafarm Products As | Method |
US8904666B1 (en) | 2011-01-04 | 2014-12-09 | Buhler Aeroglide Corporation | Dryer having hygienic panels |
NL2008383C2 (nl) * | 2012-02-29 | 2013-09-02 | Peeters Landbouwmach | Inrichting voor het mengen van materiaal en werkwijze voor het toepassen van een dergelijke inrichting. |
CN102934833B (zh) * | 2012-10-26 | 2015-11-18 | 溧阳市正申饲料机械厂 | 油脂添加器 |
US9604227B2 (en) * | 2013-06-21 | 2017-03-28 | St. Martin Investments, Inc. | System and method for processing and treating an agricultural byproduct |
US10244777B2 (en) | 2015-05-16 | 2019-04-02 | Big Heart Pet, Inc. | Palatable expanded food products and methods of manufacture thereof |
US11330833B2 (en) * | 2015-12-14 | 2022-05-17 | David J. Wise | System for delivery of biologics |
RU188043U1 (ru) * | 2018-09-05 | 2019-03-28 | Общество с ограниченной ответственностью "Машиностроительная компания "Технэкс" | Вакуумный смеситель |
JP7164420B2 (ja) * | 2018-12-07 | 2022-11-01 | ユニ・チャーム株式会社 | ペットフードの製造方法 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3467525A (en) * | 1964-12-14 | 1969-09-16 | Ralston Purina Co | Process for making an animal food |
US4393087A (en) * | 1981-05-04 | 1983-07-12 | Ralston Purina Company | Process for the production of a floating aquatic food pellet |
DK155573C (da) * | 1986-05-26 | 1989-08-14 | Jesma Matador As | Fremgangsmaade ved tilsaetning af flydende stoffer til produkter, der er fremstillet ved ekstrudering |
US4844927A (en) * | 1988-06-20 | 1989-07-04 | National By-Products, Inc. | Storage tank assembly for bulk fat and method for using same |
US4971820A (en) * | 1989-06-02 | 1990-11-20 | Canada Packers Inc. | Animal feeds and processes for their manufacture |
JP2589827B2 (ja) * | 1989-10-16 | 1997-03-12 | 日清製粉株式会社 | 多孔性養魚飼料の吸油性改良法 |
JP2721017B2 (ja) * | 1989-12-06 | 1998-03-04 | 日清製粉株式会社 | 多孔性ペレット用の液体含浸装置 |
IE61634B1 (en) * | 1990-03-12 | 1994-11-16 | David Patton Milltown Mills Li | A method of producing pelletised animal fodder |
JPH06505881A (ja) * | 1992-01-24 | 1994-07-07 | ギスト ブロカデス ナムローゼ フェンノートシャップ | 飼料ペレットの製造方法 |
-
1996
- 1996-07-22 US US09/147,400 patent/US6136353A/en not_active Expired - Fee Related
- 1996-07-22 JP JP50642098A patent/JP3985906B2/ja not_active Expired - Lifetime
- 1996-07-23 EP EP96922726A patent/EP0915664A1/fr not_active Withdrawn
- 1996-07-23 WO PCT/CH1996/000265 patent/WO1998003080A1/fr not_active Application Discontinuation
Non-Patent Citations (1)
Title |
---|
See references of WO9803080A1 * |
Also Published As
Publication number | Publication date |
---|---|
WO1998003080A1 (fr) | 1998-01-29 |
US6136353A (en) | 2000-10-24 |
JP3985906B2 (ja) | 2007-10-03 |
JP2000514655A (ja) | 2000-11-07 |
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Legal Events
Date | Code | Title | Description |
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PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
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17P | Request for examination filed |
Effective date: 19981022 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB IT LI NL SE |
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17Q | First examination report despatched |
Effective date: 20011122 |
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GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
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STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN |
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18W | Application withdrawn |
Withdrawal date: 20020531 |