WO1997028705A1 - Extruded instant granular food product - Google Patents

Extruded instant granular food product Download PDF

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Publication number
WO1997028705A1
WO1997028705A1 PCT/EP1997/000530 EP9700530W WO9728705A1 WO 1997028705 A1 WO1997028705 A1 WO 1997028705A1 EP 9700530 W EP9700530 W EP 9700530W WO 9728705 A1 WO9728705 A1 WO 9728705A1
Authority
WO
WIPO (PCT)
Prior art keywords
parts
mix
extruder
oil
powdery
Prior art date
Application number
PCT/EP1997/000530
Other languages
French (fr)
Inventor
Ernst H. Reimerdes
Original Assignee
Societe Des Produits Nestle S.A.
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=8225546&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO1997028705(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Priority to AT97902339T priority Critical patent/ATE207311T1/en
Priority to US09/125,090 priority patent/US6214406B1/en
Priority to NZ331181A priority patent/NZ331181A/en
Priority to JP9528147A priority patent/JP2000505287A/en
Priority to EP97902339A priority patent/EP0884956B1/en
Application filed by Societe Des Produits Nestle S.A. filed Critical Societe Des Produits Nestle S.A.
Priority to RU98116474/13A priority patent/RU2149571C1/en
Priority to AU16016/97A priority patent/AU717986B2/en
Priority to SK1055-98A priority patent/SK283004B6/en
Priority to CA002244233A priority patent/CA2244233C/en
Priority to DE69707649T priority patent/DE69707649T2/en
Publication of WO1997028705A1 publication Critical patent/WO1997028705A1/en
Priority to PL97328195A priority patent/PL185335B1/en
Priority to HK99102712A priority patent/HK1017589A1/en

Links

Classifications

    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS, COOKING OILS
    • A23D9/00—Other edible oils or fats, e.g. shortenings, cooking oils
    • A23D9/02—Other edible oils or fats, e.g. shortenings, cooking oils characterised by the production or working-up
    • A23D9/04—Working-up
    • A23D9/05—Forming free-flowing pieces
    • 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
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/20—Agglomerating; Granulating; Tabletting
    • 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
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/20—Agglomerating; Granulating; Tabletting
    • A23P10/22—Agglomeration or granulation with pulverisation of solid particles, e.g. in a free-falling curtain
    • 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
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/20—Agglomerating; Granulating; Tabletting
    • A23P10/25—Agglomeration or granulation by extrusion or by pressing, e.g. through small holes, through sieves or between surfaces
    • 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
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/40—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added
    • 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
    • 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
    • A23V2300/00—Processes
    • A23V2300/10—Drying, dehydrating

Definitions

  • the present invention relates to a process for the production of a free flowing and instantly dispersible and/or soluble granular food product.
  • DD-A-248502 discloses a process for the production of instant sauces or soups m the form of granules by preparing a powdery or doughlike mixture of protein hydrolysate, meat or vegetable material, instant flour or semolina, salt, sugar and spices, granulating it with a press or with an extruder, fluidised bed coating the granules with oil, carbohydrates or gums and drying them.
  • GB-A-2131271 discloses a process for the production of a granulated food based on milk or otner animal or vegetable proteins, carbohydrates, fats and minerals which comprises mixing powdery components in a fluidised bed and spraying a liquid mix of the remaining components into the powdery components, the powdery material being coated and agglomerated by the sprayed material and dried simultaneously in the fluidised bed.
  • US-A-5332585 ⁇ Odermatt et al. discloses a process for preparing a granular food product by mixing a molten fat with an amylaceous material, extruding the mixture in strands, cooling the stran ⁇ s, subdividing tne into sections and projecting the sections through a grill to reduce their into granules.
  • Tne problem addressed by tne present invention was to provide a novel and simple process for the production of a free flowing and instantly dispersible and/or soluble granular food product from carbohydrates, proteins, and oil or fats.
  • the process according to the present invention comprises preparing a mix of an oil or fats and powdery carbohydrates and/or protein rich materials in an extruder, plasticising the mix in the extruder and forming the mix into granules by extruding the plasticised mix in strands and cutting the strands.
  • the process according to the present invention indeed enables a free flowing granular food product to be produced from carbohydrates, proteins, and oil or fats which is instantly dispersible and/or soluble in warm or boiling water and which is thus suitable for the preparation of instant food in pap or liquid form.
  • stable emulsion means that a fat phase is predominantly present in form of small globules homogeneously dispersed in a liquid phase without any phase separation being observed.
  • the term "desintegrant” means a food grade desintegrating agent which is able to desintegrate the granules dispersed in water, by way of a capillarity effect, as far as the desintegrant containing granules were compacted to a certain extent during forming.
  • the present process may start from carbohydrates, proteins and/or oil or fats in form of the components of an animal or vegetable material, such as milk solids, cereal flour or soya flour, and/or in form of individual components, such as starch, polysaccharides, maltodextrines, saccharose, lactose, glucose, egg proteins, gluten, protein concentrates or protein isolates from milk, whey or soya, triglycerides of animal or vegetable origin, milk fat, palm oil, palm olein, coconut oil, or rape seed oil, for example.
  • an animal or vegetable material such as milk solids, cereal flour or soya flour
  • individual components such as starch, polysaccharides, maltodextrines, saccharose, lactose, glucose, egg proteins, gluten, protein concentrates or protein isolates from milk, whey or soya, triglycerides of animal or vegetable origin, milk fat, palm oil, palm olein, coconut oil, or rape seed oil, for example.
  • a mix which comprises, in part by weights, from 5 to 95 parts, preferably from 30 to 70 parts of carbohydrates, up to 40 parts, preferably from 15 to 30 parts of proteins, and up to 80 parts, preferably from 5 to 40 parts of oil or fats, for example.
  • emulsifier such as lecithin, mono- and/or diglycerides
  • desintegrants such as modified starches, carboxymethylcellulose (CMC) , formaldehyde-casein and other modified proteins,
  • the extruder may be a single screw or a twin screw extruder such as a MAPIMPIANTI or WENGER single screw extruder, or a BUHLER, ENGER, CLEXTRAL or WERNER & PFLEIDERER twin screw extruder, or a REA CO type TELEDYNE or AOUSTIN twin screw mixer, for example.
  • a twin screw extruder such as a MAPIMPIANTI or WENGER single screw extruder, or a BUHLER, ENGER, CLEXTRAL or WERNER & PFLEIDERER twin screw extruder, or a REA CO type TELEDYNE or AOUSTIN twin screw mixer, for example.
  • the temperature may be adjusted in different zones of the extruder in function of the work which is to be carried out in these zones, namely mixing (room temperature) , fat melting (above about 55°C) , plasticising and/or starch gelatinising (from about 120°C to about 180°C) .
  • the pressure may be adjusted accordingly from above atmospheric pressure (mixing, fat melting) up to between about 200 kPa and about 10 MPa (plasticising, starch gelatinising, extruding) , the residence time within the extruder possibly being from about 2 s to about 2 min, for example.
  • the plasticised mixture may be extruded in strands through a die such as a plate having circular openings from about
  • the extruded strands may be cut into granules from about
  • the granules thus obtained may then be dried to a residual content of between about 1 to 5%, preferably between about 2 to 3.5%, for example.
  • These granules may have a bulk density of from about 400 to 600 g/1, for example.
  • An emulsion was prepared which contained 20 parts water, 15 parts palm olein, 15 parts skimmed milk powder and 0.6 part lecithin.
  • This emulsion was fed into a twin screw extruder together with 25 parts of skimmed milk powder, 15 parts lactose and 10 parts corn starch.
  • the mix prepared in this way at room temperature in a mixing zone of the extruder was then plasticised at 140°C under 8 MPa in a mechanically compressing and shearing zone of the same extruder.
  • the plasticised mix was extruded in strands through cylindrical openings 2 mm in diameter pierced in a die plate provided at the end of the extruder.
  • the strands were cut into granules 5 mm in length which had a bulk density of 500 g/1.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Seeds, Soups, And Other Foods (AREA)
  • Dairy Products (AREA)
  • Edible Oils And Fats (AREA)
  • Confectionery (AREA)
  • Noodles (AREA)
  • Fodder In General (AREA)
  • Jellies, Jams, And Syrups (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)
  • Formation And Processing Of Food Products (AREA)
  • Fats And Perfumes (AREA)
  • Grain Derivatives (AREA)
  • Freezers Or Refrigerated Showcases (AREA)

Abstract

A process for the production of a free flowing and instantly dispersible and/or soluble granular food product, which comprises preparing a mix of an oil or fats and powdery carbohydrates and/or protein rich materials in an extruder, plasticising the mix in the extruder and forming the mix into granules by extruding the plasticised mix in strands and cutting the strands.

Description

EXTRUDED INSTANT GRANULAR FOOD PRODUCT.
The present invention relates to a process for the production of a free flowing and instantly dispersible and/or soluble granular food product.
DD-A-248502 (Institut fur Getreideverarbeitung) discloses a process for the production of instant sauces or soups m the form of granules by preparing a powdery or doughlike mixture of protein hydrolysate, meat or vegetable material, instant flour or semolina, salt, sugar and spices, granulating it with a press or with an extruder, fluidised bed coating the granules with oil, carbohydrates or gums and drying them.
GB-A-2131271 (Institut fur Getreideverarbeitung) discloses a process for the production of a granulated food based on milk or otner animal or vegetable proteins, carbohydrates, fats and minerals which comprises mixing powdery components in a fluidised bed and spraying a liquid mix of the remaining components into the powdery components, the powdery material being coated and agglomerated by the sprayed material and dried simultaneously in the fluidised bed.
US-A-5332585 {Odermatt et al.) discloses a process for preparing a granular food product by mixing a molten fat with an amylaceous material, extruding the mixture in strands, cooling the stranαs, subdividing tne into sections and projecting the sections through a grill to reduce their into granules.
Tne problem addressed by tne present invention was to provide a novel and simple process for the production of a free flowing and instantly dispersible and/or soluble granular food product from carbohydrates, proteins, and oil or fats.
To this end, the process according to the present invention comprises preparing a mix of an oil or fats and powdery carbohydrates and/or protein rich materials in an extruder, plasticising the mix in the extruder and forming the mix into granules by extruding the plasticised mix in strands and cutting the strands.
The process according to the present invention indeed enables a free flowing granular food product to be produced from carbohydrates, proteins, and oil or fats which is instantly dispersible and/or soluble in warm or boiling water and which is thus suitable for the preparation of instant food in pap or liquid form.
Throughout the present specification and claims the expression "stable emulsion" means that a fat phase is predominantly present in form of small globules homogeneously dispersed in a liquid phase without any phase separation being observed.
The term "desintegrant" means a food grade desintegrating agent which is able to desintegrate the granules dispersed in water, by way of a capillarity effect, as far as the desintegrant containing granules were compacted to a certain extent during forming.
The present process may start from carbohydrates, proteins and/or oil or fats in form of the components of an animal or vegetable material, such as milk solids, cereal flour or soya flour, and/or in form of individual components, such as starch, polysaccharides, maltodextrines, saccharose, lactose, glucose, egg proteins, gluten, protein concentrates or protein isolates from milk, whey or soya, triglycerides of animal or vegetable origin, milk fat, palm oil, palm olein, coconut oil, or rape seed oil, for example.
Thus, it is possible to prepare a mix which comprises, in part by weights, from 5 to 95 parts, preferably from 30 to 70 parts of carbohydrates, up to 40 parts, preferably from 15 to 30 parts of proteins, and up to 80 parts, preferably from 5 to 40 parts of oil or fats, for example.
The following components may be added before and/or after preparing said mix:
- up to 25 parts, preferably up to 15 parts of water,
- up to 5 parts, preferably up to 0.6 part of emulsifier, such as lecithin, mono- and/or diglycerides,
- up to 3 parts, preferably up to 1 part of desintegrants, such as modified starches, carboxymethylcellulose (CMC) , formaldehyde-casein and other modified proteins,
- up to 3 parts, preferably up to 1 part of stabilizers, such as pectine, xanthan and other gums,
- and, optionally, vitamins, micronutrients and/or antioxidants.
For preparing said mix in an extruder, it is possible to prepare an emulsion from an oil, water and an emulsifier, and to introduce simultaneously or successively said emulsion and said powdery materials into the extruder.
Alternatively it is possible to prepare a mixture of an oil or fats and powdery carbohydrates, prepare an aqueous emulsion of an oil and powdery protein materials, and introduce simultaneously or successively the mixture and the emulsicr. into the extruder.
The extruder may be a single screw or a twin screw extruder such as a MAPIMPIANTI or WENGER single screw extruder, or a BUHLER, ENGER, CLEXTRAL or WERNER & PFLEIDERER twin screw extruder, or a REA CO type TELEDYNE or AOUSTIN twin screw mixer, for example.
The temperature may be adjusted in different zones of the extruder in function of the work which is to be carried out in these zones, namely mixing (room temperature) , fat melting (above about 55°C) , plasticising and/or starch gelatinising (from about 120°C to about 180°C) . The pressure may be adjusted accordingly from above atmospheric pressure (mixing, fat melting) up to between about 200 kPa and about 10 MPa (plasticising, starch gelatinising, extruding) , the residence time within the extruder possibly being from about 2 s to about 2 min, for example.
The plasticised mixture may be extruded in strands through a die such as a plate having circular openings from about
1 to 3 mm in diameter, for example.
The extruded strands may be cut into granules from about
2 to 5 mm in length, for example.
The granules thus obtained may then be dried to a residual content of between about 1 to 5%, preferably between about 2 to 3.5%, for example.
These granules may have a bulk density of from about 400 to 600 g/1, for example.
Further forming steps such as compacting and/or spheronising may be provided for, so that the bulk density of the granules be increased up to values between about 500 and 1000 g/i, for example. An embodiment of the process according to the present invention is illustrated in the following Example in which percentages and parts are by weight.
Example
An emulsion was prepared which contained 20 parts water, 15 parts palm olein, 15 parts skimmed milk powder and 0.6 part lecithin.
This emulsion was fed into a twin screw extruder together with 25 parts of skimmed milk powder, 15 parts lactose and 10 parts corn starch.
The mix prepared in this way at room temperature in a mixing zone of the extruder was then plasticised at 140°C under 8 MPa in a mechanically compressing and shearing zone of the same extruder. The plasticised mix was extruded in strands through cylindrical openings 2 mm in diameter pierced in a die plate provided at the end of the extruder.
The strands were cut into granules 5 mm in length which had a bulk density of 500 g/1.
These granules were free flowing and instantly dispersible in warm or boiling water.

Claims

Claims
1. A process for the production of a free-flowing and instantly dispersible and/or soluble granular food product, which comprises preparing a mix of an oil or fats and powdery carbohydrates and/or protein rich materials in an extruder, plasticising the mix in the extruder and forming the mix into granules by extruding the plasticised mix m strands and cutting the strands.
2. A process as claimed m claim 1, in which said mix comprises, in parts by weights, from 5 to 95 parts of carbohydrates, up to 40 parts of proteins, and up to 80 parts of oil or fats.
3. A process as claimed in claim 2, in which the following components are added before and/or after preparing said mix:
- up to 25 parts of water, - up to 5 parts of emulsifier,
- up to 3 parts of desmtegrantε, and
- up to 3 parts of stabilizers.
4. A process as claimed in claim 1, which comprises preparing an emulsion from an oil, water and an emulsifier, and introducing simultaneously or successively said emulsion and said powdery materials into the extruder.
5. A process as claimed in claim 1, which comprises preparing a mixture of an oil or fats and powdery carbohydrates, preparing an aqueous emulsion of an oil and powdery protein materials, and introducing simultaneously or successively the mixture and the emulsion into the extruder.
PCT/EP1997/000530 1996-02-07 1997-02-06 Extruded instant granular food product WO1997028705A1 (en)

Priority Applications (12)

Application Number Priority Date Filing Date Title
DE69707649T DE69707649T2 (en) 1996-02-07 1997-02-06 EXTRUDED, GRAINY INSTANT FOOD
AU16016/97A AU717986B2 (en) 1996-02-07 1997-02-06 Extruded instant granular food product
NZ331181A NZ331181A (en) 1996-02-07 1997-02-06 Extruded instant granular food product
JP9528147A JP2000505287A (en) 1996-02-07 1997-02-06 Extruded instant granular food
EP97902339A EP0884956B1 (en) 1996-02-07 1997-02-06 Extruded instant granular food product
AT97902339T ATE207311T1 (en) 1996-02-07 1997-02-06 EXTRUDED GRANULAR INSTANT FOOD
RU98116474/13A RU2149571C1 (en) 1996-02-07 1997-02-06 Method of producing very-liquid and quick-dispersed and/or instant granular product
US09/125,090 US6214406B1 (en) 1996-02-07 1997-02-06 Method of making an extruded instant granular food product
SK1055-98A SK283004B6 (en) 1996-02-07 1997-02-06 Extruded instant granular food product
CA002244233A CA2244233C (en) 1996-02-07 1997-02-06 Extruded instant granular food product
PL97328195A PL185335B1 (en) 1996-02-07 1998-07-23 Granulated article of food
HK99102712A HK1017589A1 (en) 1996-02-07 1999-06-23 Extruded instant granular food product

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP96810080.0 1996-02-07
EP96810080A EP0796567A1 (en) 1996-02-07 1996-02-07 Granular food product

Publications (1)

Publication Number Publication Date
WO1997028705A1 true WO1997028705A1 (en) 1997-08-14

Family

ID=8225546

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP1997/000530 WO1997028705A1 (en) 1996-02-07 1997-02-06 Extruded instant granular food product

Country Status (29)

Country Link
US (2) US6214406B1 (en)
EP (2) EP0796567A1 (en)
JP (2) JPH09215486A (en)
KR (1) KR970061122A (en)
CN (2) CN1065732C (en)
AR (1) AR005760A1 (en)
AT (1) ATE207311T1 (en)
AU (2) AU725219B2 (en)
CA (2) CA2196910A1 (en)
CO (1) CO4600632A1 (en)
CZ (2) CZ33397A3 (en)
DE (1) DE69707649T2 (en)
EG (1) EG20646A (en)
HK (1) HK1017589A1 (en)
HU (1) HUP9700365A3 (en)
MA (1) MA24081A1 (en)
MX (1) MX9806054A (en)
MY (1) MY129965A (en)
NO (1) NO970384L (en)
NZ (2) NZ314191A (en)
PE (1) PE53998A1 (en)
PL (2) PL318344A1 (en)
RU (2) RU2177694C2 (en)
SG (1) SG91795A1 (en)
SK (2) SK15997A3 (en)
TR (2) TR199700088A2 (en)
TW (1) TW419356B (en)
WO (1) WO1997028705A1 (en)
ZA (1) ZA97871B (en)

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* Cited by examiner, † Cited by third party
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EP1712138A1 (en) * 2005-04-12 2006-10-18 Nestec S.A. Granulation process using microwaves

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6149957A (en) 1998-04-09 2000-11-21 Nestec S.A. Aroma recovery process
US6617446B1 (en) 1999-06-03 2003-09-09 National Starch And Chemical Investment Holding Corporation Cold water swellable starches exhibiting delayed viscosity development, preparation and use thereof
EP1074188B1 (en) 1999-08-03 2008-11-19 Société des Produits Nestlé S.A. Granular food product
ES2226628T3 (en) * 2000-03-31 2005-04-01 Societe Des Produits Nestle S.A. INSTANTANEOUS THICKENER
JP4606550B2 (en) 2000-06-09 2011-01-05 松谷化学工業株式会社 Easily dispersible soybean protein granule and method for producing the same
US6716466B2 (en) 2001-01-17 2004-04-06 Nestec S.A. Balanced food powder composition
US6514546B2 (en) 2001-01-31 2003-02-04 Koji Tsukuda Easily dispersible granules of soybean protein and methods for preparing the same
AU2002352153A1 (en) * 2001-12-21 2003-07-09 Unilever N.V. Instant emulsion
US7445807B2 (en) * 2002-10-15 2008-11-04 Western Holdings, Llc Agglomerated granular protein-rich nutritional supplement
US7387795B2 (en) * 2003-06-05 2008-06-17 Jane Hollenberg Cosmetic compositions organophosphonic acid coated particulates and methods for producing the same
EP1651338B1 (en) 2003-07-17 2011-05-18 Unilever N.V. Process for the preparation of an edible dispersion comprising oil and structuring agent
US20050058766A1 (en) * 2003-09-11 2005-03-17 Han Chung Wan Anti-diabetic diet and method for providing a proportioned ground food
WO2006010053A1 (en) * 2004-07-07 2006-01-26 Archer-Daniels-Midland Company Low carbohydrate flour additive
AU2006215830B2 (en) 2005-02-17 2010-03-04 Upfield Europe B.V. Fat granules
ES2385397T5 (en) * 2005-03-04 2015-08-10 Dsm Ip Assets B.V. Particle lipid composition for food products
BRPI0609024A2 (en) * 2005-03-08 2010-01-12 Nestec Sa extruded solid product for use in food products
US20070009639A1 (en) * 2005-06-30 2007-01-11 Schuppan Robert L Barrier for food particles
CA2685936C (en) * 2007-05-07 2016-07-12 Clearly Superior, Inc. Food thickening agent, method for producing food thickening agent
JP2008295380A (en) * 2007-05-31 2008-12-11 Ikari Super Market:Kk Foodstuff containing gaba and its preparation method
ATE510459T1 (en) * 2008-02-19 2011-06-15 Nestec Sa FOOD CAPSULE
US8865245B2 (en) 2008-12-19 2014-10-21 Conopco, Inc. Edible fat powders
US9131710B2 (en) 2009-03-02 2015-09-15 Roquette Freres Vegetable milk granulated powder, process for producing vegetable milk, and uses thereof
FR2942586B1 (en) * 2009-03-02 2011-05-13 Roquette Freres GRANULATED POWDER CONTAINING PLANT PROTEINS AND MALTODEXTRINS, PROCESS FOR OBTAINING THEM AND USES THEREOF
MX2012014850A (en) * 2010-06-14 2013-05-01 Abbott Lab Ultrasonically-assisted extrusion methods for manufacturing powdered nutritional products.
AU2011269239B2 (en) 2010-06-22 2014-03-06 Upfield Europe B.V. Edible fat powders
PL2651234T3 (en) * 2010-12-17 2015-06-30 Unilever Bcs Europe Bv Process of compacting a microporous fat powder and compacted fat powder so obtained
EP2651229B1 (en) 2010-12-17 2015-04-08 Unilever N.V. Edible water in oil emulsion
JP5879658B2 (en) * 2011-09-05 2016-03-08 倉田　勇雄 Method for producing tablet-like food
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WO2014066680A1 (en) * 2012-10-24 2014-05-01 Abbott Laboratories Use of extrusion methods to improve heat labile vitamin stability
US20140170265A1 (en) * 2012-12-19 2014-06-19 Mead Johnson Nutrition Company Infant formula cubes
EP2983501A1 (en) * 2013-03-12 2016-02-17 Abbott Laboratories Microbial reduction in nutritional product using an extrusion process
US9101156B2 (en) 2013-03-15 2015-08-11 Kent Precision Foods Group, Inc. Thickener composition, thickened nutritive products, methods for preparing thickened nutritive products, and methods for providing nutrition
WO2015171906A1 (en) * 2014-05-08 2015-11-12 Abbott Laboratories Extruded powder nutritional composition and methods of producing same
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4811031B1 (en) * 1970-12-18 1973-04-10
US4532146A (en) * 1979-09-19 1985-07-30 Fromageries Bel Milky products for manufacturing chocolate-trade products and method or preparation thereof
JPS61260837A (en) * 1985-05-15 1986-11-19 Tech Res Assoc Extru Cook Food Ind Production of rice cake
EP0490082A1 (en) * 1990-12-07 1992-06-17 Societe Des Produits Nestle S.A. Granulated base material for sauces and soups
EP0509748A1 (en) * 1991-04-16 1992-10-21 Bocm Pauls Limited Process for the manufacture of compound animal feedstuffs
EP0594152A2 (en) * 1992-10-21 1994-04-27 House Food Industrial Co., Ltd. Method for preparing granular foods

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1203715A (en) * 1957-12-09 1960-01-20 Carnation Co Powdered soup and its production process
US3142569A (en) * 1960-11-23 1964-07-28 Koopmans Meelfabrieken N V Process for preparing powdered foodstuff containing finely dispersed fat
FR1348948A (en) * 1963-02-28 1964-01-10 Procter & Gamble Process for the agglomeration of powdered food mixtures containing flour
JPS4921072B1 (en) * 1970-05-18 1974-05-29
JPS58107152A (en) * 1981-12-16 1983-06-25 Meiji Seika Kaisha Ltd Preparation of granular curry roux
DD228951A3 (en) * 1982-12-02 1985-10-23 Inst Getreideverarbeitung PROCESS FOR PRODUCING GRANULATED FOOD
JPS60145055A (en) * 1984-01-10 1985-07-31 House Food Ind Co Ltd Preparation of food containing granular fats and oils
US4585657A (en) * 1984-12-14 1986-04-29 Nabisco Brands, Inc. Agglomerated flavor bits
DD248502A1 (en) * 1984-12-28 1987-08-12 Inst Getreideverarbeitung PROCESS FOR THE PRODUCTION OF COOKED SOUPS AND BRANDICAS
KR880002455A (en) * 1986-08-23 1988-05-09 이홍희 Manufacturing method of instant powder food
JPS63186799A (en) * 1987-01-29 1988-08-02 不二製油株式会社 Production of powdery oils and fats
US5540944A (en) * 1994-09-30 1996-07-30 Nestec S.A. Process of preparing a film-coated meat product
EP0825819B1 (en) * 1995-03-31 2003-10-01 Cereal Ingredients, Inc. Method of flavoring and texturizing food particles and product thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4811031B1 (en) * 1970-12-18 1973-04-10
US4532146A (en) * 1979-09-19 1985-07-30 Fromageries Bel Milky products for manufacturing chocolate-trade products and method or preparation thereof
JPS61260837A (en) * 1985-05-15 1986-11-19 Tech Res Assoc Extru Cook Food Ind Production of rice cake
EP0490082A1 (en) * 1990-12-07 1992-06-17 Societe Des Produits Nestle S.A. Granulated base material for sauces and soups
US5332585A (en) * 1990-12-07 1994-07-26 Nestec S.A. Preparation of a granular food product
EP0509748A1 (en) * 1991-04-16 1992-10-21 Bocm Pauls Limited Process for the manufacture of compound animal feedstuffs
EP0594152A2 (en) * 1992-10-21 1994-04-27 House Food Industrial Co., Ltd. Method for preparing granular foods

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Week 7315, 1973 Derwent World Patents Index; AN 73-20995u, XP002005986 *
DATABASE WPI Week 8701, 1987 Derwent World Patents Index; AN 87-002389, XP002005987 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1712138A1 (en) * 2005-04-12 2006-10-18 Nestec S.A. Granulation process using microwaves

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