CA2171762A1 - Expanded coating material - Google Patents

Expanded coating material

Info

Publication number
CA2171762A1
CA2171762A1 CA002171762A CA2171762A CA2171762A1 CA 2171762 A1 CA2171762 A1 CA 2171762A1 CA 002171762 A CA002171762 A CA 002171762A CA 2171762 A CA2171762 A CA 2171762A CA 2171762 A1 CA2171762 A1 CA 2171762A1
Authority
CA
Canada
Prior art keywords
protein
dough
starch
less
temperature
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.)
Abandoned
Application number
CA002171762A
Other languages
French (fr)
Inventor
Godelieve Johanna Maria Bun
Frankwin Van Dieren
Glenda Lesley Scott
Richard William F. Yoell
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.)
Unilever PLC
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of CA2171762A1 publication Critical patent/CA2171762A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L17/00Food-from-the-sea products; Fish products; Fish meal; Fish-egg substitutes; Preparation or treatment thereof
    • A23L17/75Coating with a layer, stuffing, laminating, binding or compressing of original fish pieces
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, 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
    • A23L7/00Cereal-derived products; Malt products; Preparation or treatment thereof
    • A23L7/10Cereal-derived products
    • A23L7/157Farinaceous granules for dressing meat, fish or the like

Abstract

A novel, smooth coating material having a defined shape and an advantageously low oil uptake on deep-frying is made by: (a) extruding a dough comprising from 10 to 60 % by dry weight protein and from 90 to 40 % by dry weight starch through an approximately shaped die; providing that when the dough comprises from 30 to 60 % protein, the dough is extruded at a temperature of from 60 to 100 .degree.C; and when the dough comprises below 30 % protein, the protein is substantially a fast hydrating protein and the dough is extruded at a temperature of less than 40 .degree.C; (b) cutting the appeanng extrudate into approximately equally thick sections to form a shaped pellet; and (C) expanding the pellet, preferably by frying in oil.

Description

W095/07629 PCT~P94/02998 ~ 217~2 Expanded coating mater~al.

FIELD OF THE INVENTION

The invention relates to a coating material for ~ood products having a novel defined, smooth shape and an advantageously low oil uptake on deep-frying, a method of preparing such coating materials and a food product coated with such a coating material.
BACKGROUND AND PRIOR ART

There is a continuing need of coated food products such as coated meat, poultry, vegetables or fish. Usually, these coated food products are obtained by first wetting a raw or at least partially cooked, optionally frozen, product, for instance by glazing or dipping into, or spraying with, a fluid substance such as water or batter and, subsequent to wetting, applying a particulate breading material. If desired, the steps of wetting and breading can be repeated to obtain a multi-layered coating. Before storage, the coating is pre-set, for instance by pre-frying.

Well known crumb coating materials contain particles of a heat-treated starchy material. Several methods for obtaining these materials have been known for a long time.
One of these methods involves the baking of a loaf of bread which, after staling, is ground into conventional bread crumbs. Another method involves the cooker extrusion of a mixture of flour and water, the extrudate then being ground for instance to obtain so-called Japanese crumbs.

The crumb coatings obtained thereby have a sandy irregular appearance. These crumb coatings absorb a substantial amount of oil when the coated food product is deep-fat fried. Furthermore, although by the provision of Japanese crumb comprising differently coloured particles more -W095/07629 PCT~P94/02998 ~ ~ 7 ~ 2 variety in appearance is provided, there is a continuing need ~or more variety.

US 4 568 550 (General Foods Corp) discloses extruding a dough having a moisture content of 20 to 40~ at 60C to 120C while under pressures and low shear conditions and for a period of time effective to set the protein and to partially gelatinise the starch in the flour while maint~;ning the starch granule integrity. The extrudate is then subjected to the appropriate conditions in order to puff and expand extrudate. The puffing explodes the extrudate to provide the required aerated breadlike structure. This process therefore teaches away from providing a smooth, shape-retained extrudate.
It is therefore an object of this invention to provide a novel shaped particulate coating material having a defined smooth shape and a low oil uptake when deep-fried.

DEFINITION OF THE INVENTION

Accordingly the invention provides a crisp particulate coating material having a defined smooth shape and an oil uptake of less than 40~ by weight of the crumb composition, comprising from 90-40~ starch and from 10 to 60~ protein, providing that when the protein content is less than 30~ by dry weight the protein is a fast hydrating protein.

The invention also provides a method of manufacturing a particulate coating material having a defined, smooth shape and an oil uptake of less than 40~ by weight of the crumb composition, comprising:

a) extruding a dough comprising from 10 to 60~ by dry weight protein and from 90 to 40~ by dry weight starch through an appropriately shaped die; providing that when the dough comprises from 30 to 60~ protein, the dough is 2~7~76~
W095/07629 PCT~P94102998 extruded at a temperature of from 60 to 100C; and when the dough comprises below 30~ protein the protein is substantially a fast hydrating protein and the dough is extruded at a temperature of less than 40C;
b) cutting the appearing extrudate into approximately equally thick sections to form a shaped pellet; and c) a means to effect expansion of the pellet.

The invention further provides a food product comprising an edible core and a coating of such defined smooth shaped particles as described above.

By oil uptake is meant the percentage of oil absorbed/retained by the crumb composition during the process of frying in oil in order to cook the crumb coated foodstuff. Preferably the crumb has an oil uptake of less than 30~ most preferably less than 25~.
By defined shape is meant that the particulate coating material has undergone no puffing of its structure during manufacture, in other words the original shape of the coating material has been retained during its manufacture.
By fast hydrating protein is meant a protein that is fully hydrated after 2 to 5 minutes at room temperature.

The dough composition is manufactured by a~m;~ng the re~uired particulate ingredients with water, and preferably has a moisture content of from 23 to 45~. A dough having a protein content of from 30-60~ more preferably has a moisture content from 25 to 40~, even more preferably from 28 to 33~, most preferably 30~. A dough having a protein content of less than 30~ more preferably has a moisture content of from 35 to 45~.

W095/07629 PCT~P9~/02998 .

7 ~ 4 The particulate components thus comprise starch and protein in a ratio of from 9:1 to 2:3. If the protein content is not fast hydrating protein the preferred ratio of starch to protein is from 2:1 to 2:3 most preferably 3:2 to 1:1. If the protein content is substantially fast hydrating protein the preferred ratio of starch to protein is from 4:1 to 7:1.

Suitable proteins include vegetable proteins for example soya protein, chick pea protein and particularly includes cereal proteins such as vital wheat gluten.

Suitable starches include vegetable starches for example potato starch and particularly includes cereal starches, for example wheat starch, maize starch and rice starch.
Preferably the starch is a waxy maize starch.

Since starch and protein are present in flours, such flours, for example cereal flour, may therefore be utilised with or without further starch and/or protein addition in order to obtain the desired ratio of starch to protein, for manufacture of the dough. In particular the flour may be Canadian Wheat Red Springs flour (CWRS).

Further optional ingredients which may be included in the crumb coating include for example salt, flavouring materials, fillers, vegetable particles, sugar, fats, emulsifiers, colours, gasifying agents, food fibres and bran.
When the protein content of the dough is from 30 to 60~, the dough is extruded through an appropriately shaped die at a temperature of from 60 to 100C, preferably from 65 to 80C, most preferably 70C.
When the protein content of the dough is less than 30~, the dough is extruded through an appropriately shaped die at a 217~7~2 W095/07629 PCT~P94/02998 temperature of less than 40C, preferably less than 30C.

The means to effect expansion of the shaped pellet, may be any suitable means known to the man skilled in the art.
Preferably expansion is effected via heat treatment.

The heat treatment may preferably be selected from frying in oil, heating in a hot air oven and microwaving. Most preferably the expansion is effected by frying the dried pellets in oil at preferably 170C to 220C until suitably expanded.

Additionally a drying step may be incorporated into the manufacturing method detailed above after step (b) whereby the shaped pellets are dried to a moisture content of from 5 to 30~. This is particularly advantageous when the moisture content of the dough prior to extrusion is greater than 35~ because it prevents the shaped pellets from sticking together. If the protein content of the dough is from 30 to 60~ the shaped pellets are preferably dried to a moisture content o~ from 10 to 20~ and more preferably 15~. Whereas if the protein content of the dough is less than 30~, the shaped pellets are preferably dried to a moisture content of from 22 to 25~.
The cross section of the die will determine the final shape of the crumb and may be any desired shape. However, it is preferred that the final crum.b size does not exceed 12 mm and more preferably does not exceed 10 mm. Particularly suitable m~;ml~m ~;mPn~ions being from 3 to 8 mm having a sufficiently large size to have definition and not too large to be inconvenient when cutting or biting the final crumb product.

W 095/07629 PCT~EP9~/02998 ~ 7 ~ 6 USE OF THE CRUM~ COATING COMPOSITION

Crumb coating compositions according to the invention may be used to provide ~ood products such as coated meat, poultry, vegetables or ~ish. J

The crumb coating is preferably applied to a ~ood substance which has ~irst been wetted by glazing or dipping into, or spraying with, a ~luid substance such as water or batter.
The coating may be pre-set, ~or instance by pre-~rying.

Food products coated with the crumb coating according to the invention, on heating for consumption, have a desirable crisp crumb coating, and a novel shape.
EXAMPLES

The invention will be ~urther illustrated by the ~ollowing examples. All parts and percentages are by weight unless otherwise indicated.

Examples 1-4 : Comparative Examples A-C

A dough was prepared comprising vital wheat gluten, waxy maize starch, salt and water in the proportions shown in Table 1.

Table 1 ~ By Weight of Composition Example Protein Starch Salt Water ' 1 22.8 45.7 1.5 30.0 2 41.1 68.5 1.5 30.0 3 34.25 34.25 1.5 30.0 35 4 68.5 41.1 1.5 30.0 A 17.1 51.4 1.5 30.0 B 45.7 22.8 1.5 30.0 C 51.4 17.1 1.5 30.0 2~ 71 762 W095/07629 PCT~P941029~8 .

The dough was extruded through a shaped die of a CLEXTRAL
BC 45 cooker extruder at a temperature of 70C. The die was star-shaped having an 8mm diameter. The appearing strand was cut into 2mm thick shaped pellets. These were dried at 70C to a moisture content of 15~. The shaped pellets were then fried in hot oil at about 170 for 30 to 40 seconds.

Fish fingers in a frozen condition were coated with a fluid batter of the following composition:

45 parts flour 3 parts NaCl 52 parts water Thereafter the fried coating particles were coated all around the battered fish fingers, whereafter the coated fingers were flash fried by immersing 20 seconds in hot oil at about 190 to 195C.
The crumb coating had the properties shown in Table 2. The measurements were made after cooking the fish fingers in oil for consumption.

Example Crumb coating characteristics ~ fat uptake 1 smooth, shape-retained crisp 20 2 smooth, shape-retained, crisp,20 firm 3 smooth, shape-retained, crisp,22 firm 4 shape-retained, crisp, firm 20 A smooth, shape-retained, not 25-30 crisp starchy, fragile B slightly rough, firm, crisp ~40 C very rough and hard, no shape,40 retention W095/07629 PCT~P94/029g8 .

2.~7~7~ 8 It was observed that the higher the protein content, the rougher and ~irmer the crumb becomes and also the crumb ~pu~fs" more on cooking and hence does not retain its shape. This results in a higher ~at uptake on deep-fat frying. The higher the starch content, the smoother the crumb becomes and the better it retains its shape. However too high a starch content provides a more fragile crumb into which the oil can penetrate more easily, resulting in a higher ~at uptake.

Examples 5-10 A dough was prepared comprising CWRS flour having a moisture content of 40~. The CWRS ~lour had a starch content of 85~ and a protein content of 15~. The protein was fast hydrating protein.

The dough was extruded through a shaped die of a CLEXTRAL
BC 45 cooker extruder at a temperature of 33C. The die was star shaped and had an 8mm diameter. The appearing strand was cut into 2mm thick shaped pellets and ;mm~;ately dried under the conditions shown in Table 3. The shaped pellets were then fried in hot oil at about 190C for 60 seconds.

25 Table 3 Example Drying temp Moisture content Fat after drying Uptake 40C 15~ 20 6 40C 18~ 17.4 7 70C 17~ 21 8 70C 19~ 19 9 40C 24.8~ 24.1~
40C 29.0~ 27.6~ -All crumbs were smooth, shape-retained and crisp. Example 6 crumbs were the most crisp.

wosS/07629 2 ~ 1 l 1 6 2 PCT~P94/02998 .

Comparative Example D

Fish fingers were coated with a fluid batter as for Example 1. Thereafter the fish fingers were coated with commercially available Pandora Crumb, whereafter the coated fingers were flash fried by immersing 20 seconds in hot oil of about 190 to 195C before cooking the fish fingers in oil for consumption. The fat uptake of the crumb was greater than 50~.

Claims (16)

1. A method of manufacturing a particulate coating material having a defined, smooth shape and an oil uptake of less than 40% by weight of the crumb composition, comprising:

a) extruding a dough comprising from 10 to 60% by dry weight protein and from 90 to 40% by dry weight starch through an appropriately shaped die; providing that when the dough comprises from 30 to 60% protein, the dough is extruded at a temperature of from 60 to 100°C; and when the dough comprises below 30% protein the protein is substantially a fast hydrating protein and the dough is extruded at a temperature of less than 40°C;

b) cutting the appearing extrudate into approximately equally thick sections to form a shaped pellet; and c) a means to effect expansion of the pellet.
2. A method according to claim 1 wherein the dough has a moisture content before extrusion of from 23% to 45%.
3. A method according to claim 1 or 2 additionally comprising a drying step whereby the shaped pellets are dried to a moisture content of from 5 to 30% prior to expansion.
4. A method according to any preceding claim wherein the protein is a cereal protein.
5. A method according to any preceding claim wherein the starch is a cereal starch.
6. A method according to any preceding claim comprising:

a) extruding a dough comprising starch and protein in a ratio of from 2:1 to 2:3 at a temperature of from 60 to 100°C through an appropriately shaped die;

b) cutting the appearing extrudate into approximately equally thick sections to form a shaped pellet; and c) effecting expansion of the pellet.
7. A method according to claim 6 wherein the ratio of starch to protein is from 3:2 to 1:1.
8. A method according to claim 6 or 7 wherein the dough is extruded at a temperature of from 65 to 80°C.
9. A method according to claim 6, 7 or 8 wherein the dough has a moisture content before extrusion of from 25 to 40%.
10. A method according to any one of claims 6 to 9 wherein the dough has a moisture content before extrusion of from 28 to 33%.
11. A method according to any one of claims 1 to 5 comprising:

a) extruding a dough comprising less than 30% protein, wherein substantially all the protein is a fast hydrating protein, at a temperature of less than 40°C through an appropriately shaped die;

b) cutting the appearing extrudate into approximately equally thick sections to form a shaped pellet; and c) effecting expansion of the pellet.
12. A method according to claim 11 wherein the ratio of starch to protein is from 4:1 to 7:1.
13. A method according to claim 11 or 12 wherein the dough is extruded at a temperature of less than 30°C.
14. A method according to claim 11, 12 or 13 wherein the dough has a moisture content before extrusion of from 35 to 45%.
15. A particulate coating material having a defined smooth shape and an oil uptake of less than 40% by weight of the crumb composition comprising from 10 to 60% by dry weight protein and from 90 to 40% by dry weight starch, providing that when the protein content is less than 30%, substantially all the protein is a fast hydrating protein.
16. A particulate coating material having a defined smooth shape and an oil uptake of less than 40% by weight of the crumb composition obtainable by:

a) extruding a dough comprising from 10 to 60% by dry weight protein and from 90 to 40% by dry weight starch through an appropriately shaped die; providing that when the dough comprises from 30 to 60% protein, the dough is extruded at a temperature of from 60 to 100°C; and when the dough comprises below 30% protein the protein is substantially a fast hydrating protein and the dough is extruded at a temperature of less than 40°C;

b) cutting the appearing extrudate into approximately equally thick sections to form a shaped pellet; and c) a means to effect expansion of the pellet.
CA002171762A 1993-09-14 1994-09-08 Expanded coating material Abandoned CA2171762A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP93307241 1993-09-14
EP93307241.5 1993-09-14

Publications (1)

Publication Number Publication Date
CA2171762A1 true CA2171762A1 (en) 1995-03-23

Family

ID=8214542

Family Applications (1)

Application Number Title Priority Date Filing Date
CA002171762A Abandoned CA2171762A1 (en) 1993-09-14 1994-09-08 Expanded coating material

Country Status (12)

Country Link
EP (1) EP0719096A1 (en)
JP (1) JPH09502356A (en)
AU (1) AU7656694A (en)
CA (1) CA2171762A1 (en)
CZ (1) CZ76596A3 (en)
HU (1) HUT73944A (en)
PL (1) PL313477A1 (en)
SG (1) SG82557A1 (en)
SK (1) SK33196A3 (en)
TW (1) TW284673B (en)
WO (1) WO1995007629A1 (en)
ZA (1) ZA947004B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6645541B2 (en) 2000-09-27 2003-11-11 Wynn Starr Flavors, Inc. Enhancing puffable food products and for production thereof
US20030039735A1 (en) * 2000-09-27 2003-02-27 Kazuaki Morii Gelatinized potato starch breading composition and process for manufacture
JP4735583B2 (en) * 2007-03-27 2011-07-27 不二製油株式会社 Fry food glaze
GB2461520A (en) 2008-07-01 2010-01-06 Magsnack Bv Manufacturing crumb for the coating of food products
GB201000647D0 (en) 2010-01-15 2010-03-03 Crisp Sensation Holding Sa Microwaveable batter
US8765202B2 (en) 2010-01-15 2014-07-01 Crisp Sensation Holding S.A. Coated stabilised microwave heated foods
US9326536B2 (en) 2011-01-27 2016-05-03 Crisp Sensation Holding S.A. Production of microwaveable coated food products
US9326537B2 (en) 2011-01-27 2016-05-03 Crisp Sensation Holding S.A. Microwaveable coated food product, and method and apparatus for the manufacture thereof
WO2012110972A1 (en) * 2011-02-16 2012-08-23 Finecrumb Food Coatings (Proprietary) Limited A method of producing an extruded breadcrumb coating for food products
US20130156925A1 (en) 2011-12-20 2013-06-20 Crisp Sensation Holding S.A. Crumb manufacture

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3753728A (en) * 1970-10-05 1973-08-21 Procter & Gamble Process for production of soy-containing breakfast cereals
US3814824A (en) * 1971-06-28 1974-06-04 Procter & Gamble Breakfast cereals containing soy material and sodium bicarbonate
US3873748A (en) * 1973-07-02 1975-03-25 Gen Mills Inc Process for making high-protein cereal
FR2401615A1 (en) * 1977-08-29 1979-03-30 Sodes Sa Food prods contg. bran, gluten and flour - prepd. continuously by extruding mixt. with water; used in diet bread, cereals, etc.
US4568550A (en) * 1981-09-08 1986-02-04 General Foods Corporation Process for preparing a cooked extruded flour-based product
ES2042769T3 (en) * 1987-12-03 1993-12-16 Unilever Nv GROCERIES.
JPH0842B2 (en) * 1992-04-10 1996-01-10 ユニリーバー・ナームローゼ・ベンノートシヤープ Edible crisp material and method for producing the same

Also Published As

Publication number Publication date
EP0719096A1 (en) 1996-07-03
CZ76596A3 (en) 1996-08-14
JPH09502356A (en) 1997-03-11
HUT73944A (en) 1996-10-28
TW284673B (en) 1996-09-01
HU9600634D0 (en) 1996-05-28
SK33196A3 (en) 1996-09-04
SG82557A1 (en) 2001-08-21
WO1995007629A1 (en) 1995-03-23
PL313477A1 (en) 1996-07-08
ZA947004B (en) 1996-03-12
AU7656694A (en) 1995-04-03

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