CA1115115A - Corn bran expanded cereal - Google Patents
Corn bran expanded cerealInfo
- Publication number
- CA1115115A CA1115115A CA349,928A CA349928A CA1115115A CA 1115115 A CA1115115 A CA 1115115A CA 349928 A CA349928 A CA 349928A CA 1115115 A CA1115115 A CA 1115115A
- Authority
- CA
- Canada
- Prior art keywords
- percent
- corn bran
- ground
- product
- cereal
- 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.)
- Expired
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/161—Puffed cereals, e.g. popcorn or puffed rice
- A23L7/165—Preparation of puffed cereals involving preparation of meal or dough as an intermediate step
- A23L7/17—Preparation of puffed cereals involving preparation of meal or dough as an intermediate step by extrusion
Abstract
ABSTRACT OF THE DISCLOSURE
An extruded, expanded ready to eat cereal product containing substantial levels of corn bran is disclosed. Ex-plosive expansion of the cereal dough with sudden release of pressure in the cooking extrusion step results in a high de-gree of cereal piece disintegration unless the corn bran in-gredient which is used in the process is within critical par-ticle size ranges. Product produced in accordance with the invention has preferred sensory qualities when compared with wheat bran. A high fiber expanded ready to eat product having improved textural and bowl life characteristics, compared to commercially available ready to eat cereals containing wheat bran, is disclosed.
An extruded, expanded ready to eat cereal product containing substantial levels of corn bran is disclosed. Ex-plosive expansion of the cereal dough with sudden release of pressure in the cooking extrusion step results in a high de-gree of cereal piece disintegration unless the corn bran in-gredient which is used in the process is within critical par-ticle size ranges. Product produced in accordance with the invention has preferred sensory qualities when compared with wheat bran. A high fiber expanded ready to eat product having improved textural and bowl life characteristics, compared to commercially available ready to eat cereals containing wheat bran, is disclosed.
Description
~:
The present invention relates to a dry ready to eat high fiber cereal and a process of preparing the same.
Recently, there has developed increasing in-terest among nutritionists and among consumers in~high fiber food products, particularly in high fiber ready to eat cereals. At the present time, wheat bran is the principal ingredient which is relied upon to provide high fiber content for example in ready to eat cereals. How-ever, some commercially available wheat-bran ready to eat cereal products become soggy and pasty almost immediately upon wetting of the product in milk. Others are very hard and go almost to the other extreme of not being palatable, even in milk, because of prolonged hardness.
On the other hand vast quantities of maize corn bran are avaiable for use in the high fiber human food products such as, for example, ready to eat cereals. It would be highly desirable to produce high fiber cereal products utilizing maize corn bran as the source for the high fiber content, in conventional cooker-extruder ex-pansion processes and equipment, such as those disclosed in U.S. Patent 3,054,677 to W. R. Graham, Jr. et al.
or U.S. Patent 3,462,277 to R. R. Reinhardt. Such processes and equipment economically and at very high speeds, produce a modern dry, ready to eat cereal pro-duct, having an attractive palatable appearance, e.g., a bite size or larger sized product, having strong sales .
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; . ,' . :
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appeal to the average consumer. The products are light, crisp and frangible, having pleasing color and taste.
In such processes a dry-appearing mixture of in-gredients is passed quickly through a cooker-extruder in which high pressure and temperature is generated. The ingredients are quickly cooked, a dough is formed, and the dough is expelled through a constricted opening, e.g.
through a plurality of dies, under high temperature and pressure conditions. Temperature and pressure ahead of the dies are maintained high enough to cause sudden release of pressure when the dough is forced through the dies, with sudden conversion of at least some of the mois-ture to steam in the extruded dough mass to develop small and large bubbles in the resulting product. This develop-ment of bubbles throughout the extrudate is called "ex-pansion." The extruded expanded dough passes through a momentary, fleeting stage in which the dough is extremely cohesive, sticky and flexible, and upon the sudden flash-ing of some additional amounts of the water, the water content drops, and the pieces are immediately transformed into less sticky pieces. The pieces are then typically charged into a high temperature, high velocity air stream, in which the drying step is completed and the dry pieces develop the highly desirable toasted appearance.
: However, the technology has not been available for the production of an extruded expanded cereal product using maize corn bran as an ingredient in such processes.
It is an object of the present invention to pro-vide process technology for the production of extruded expanded ready to eat cereal products utilizing maize corn bran as an ingredient, which product has very favorable sensory characteristics. It is a further object of the present invention to provide a high fiber expanded ready to eat cereal product utilizing maize corn bran as the principal source of the additional fiber present.
The present invention provides a process for producing a dry ready to eat high fiber cereal product comprising the steps: admixing with cereal dough ingred-ients sufficient ground maize corn bran, as an ingredient, to provide a fiber content of 3.5 to 10% by weight, based on the weight of the product, said ground maize corn bran having been ground to a fineness whereby 100 percent ofsaidgroundmaize corn passes through a 40 mesh U.S.
sieve, cooking the ingredients in a cooker-extruder to form an extrudate under temperature and pressure conditions sufficiently high to result in expansion of the dough upon its release from the cooker-extruder, cutting the expanded dough extrudate into discrete pieces, and drying the resulting pieces to a moisture level of 2-3 percent.
The present invention further provides a dry ready to eat expanded cereal product produced in a cooker-extrusion expansion process, said cereal including ground maize corn bran in an amount sufficient to provide 3.5 -10.0 percent inclusive fiber content, by weight based on the weight of the product, said ground maize corn bran having been added to said product as an ingredient which wasground to a fineness whereby 100 percent of said ground maize corn bran passes through a 40 mesh U.S. sieve.
In accordance with the present invention, an extruded expanded ready to eat cereal product utilizing maize corn bran as an ingredient to supply additional fiber, is produced in an otherwise conventional cooker-extrusion expansion p.rocess, but wherein the maize corn bran ingredient has been ground to a granulation of at least 100 percent through a 40 mesh U.S. sieve. In one preferred aspect maize corn bran ingredients having a granulation of 100 percent through a 60 mesh U.S. sieve and 70 percent through 100 mesh U.S. sieve are employed. None-theless, another preferred embodimentutilizes a granu-lation such that 100 percent passes through 40 mesh, and 45 percent stays on a 60 mesh U.S. sieve. Although I have discovered that there is no limit with respect to the amount of extremely fine particles, in fact for economic . .
,i reasons I prefer to use ingredients in which substantial portion thereof, e.g. 40 percent remains on a 60 mesh sieve.
I have found that the improved process, in ac-cordance with the present invention, is suitable for use with any type of cooked cereal dough ingredients, and in any process which utilizes a cooker-extruder, and which produces an expanded cereal product upon sudden release of pressure from the extruder through a die. There are many such processes widely known in the art, and for ex-ample those set forth in the above cited patents, and a wide range of densities are achieved in the resulting products due to the expansion into steam of the rela-tively low levels of water which are present in the dough in the extruder cooker.
Utilization of maize corn bran straight from the dry milling process in such processes was found to be totally unworkable. Such ingredients cause erratic plug-ging of the dies, surging of the dough through the extrud-er and orifices, and most significantly, results in extreme cereal piece disintegration during and after expansion.
Furthermore, coarse grinding of the maize corn bran, e.g.
so that a major portion of the ground bran just passes through 2 or 4 mesh U.S. sieve, although improving the orifice plugging problem, nonetheless results in unaccept-able surging, as well as product disintegration during and immediately after expansion. We have found that when the maize corn bran is ground to fineness at or finer than the ; levels set forth above, the orifice extrusion problem is totally eliminated, the surging problem is totally elim-inated, and the product disintegration problem during and after expansion is also eliminated. In addition, we have discovered that the resulting product has scored better than commercially available high fiber wheat-bran derived cereals when compared in consumer tests.
In the following examples all parts are expressed in parts by weight, and temperatures are expressed in degrees Fahrenheit.
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The ingredients set forth below in Table 1 were added to a ribbon blender in the relative amounts set ` ~ forth, and were mixed until the contents of the blender appeared to be homogenous.
Yellow Maize Corn Flour 49.9 %
Ground Maize Corn Bran 25.00%
; Oat Flour 15.00%
Sugar 8.0 %
Salt 1.0 %
Soda 0-75%
Vitamin Premix 0.15~
Ground Limestone 0.17%
Color (brown) 0.02%
",~ 100. 00%
*The ground maize corn bran is maize corn bran that has been ground to a granulation of 100 percen$
through 40 mesh U.S. sieve with 45 percent on 60 ~ mesh U.S. sieve.
h +giving a fiber content of approximately 3.5~ of the whole mix.
The resulting mixture was found to contain ap-proximately 8 percent moisture. The resulting admixture is, in a separate blender, further admixed with additional quantity of makeup water so that the resulting admixture consists of approximately 20 percent total moisture. The resulting 20 percent moisture mix is freeflowing although ` it does give evidence of cohesion upon in-hand compression.
The 20 percent moisture mix is charged to an extruder cooker in which both the extruder and propulsion screw are equipped internally for water cooling. Room temperature water is circulated through both~the jacket and the screw and approximately a 10F. increase in temp-erature is encountered on the jacket although the screw coolant water exited at approximately 115 F. The extruder cooker is operated in a conventional manner to provide compression, propulsion, and extrusion of the dough, under conditions such that even though cooling is applied, the dough temperature upon extrusion is approxi-mately 340~F. with the sudden release of pressure. For example, the extrudate is passed through six orifices closely arranged in a circle in the die base and the ex-trudate from each respective orifice contacts and co-heres to extrudate on either side to form a tube. The tube is allowed to pass between conventional cutting rolls to result in individual pillow shape pieces. Typical conventional extrusion, and cutting equipment which is suitable for use in accordance with the present invention is shown in U.S. Patent 3,054,677 to W. R. Graham, Jr.
et al.
Upon the cutting of the product into pieces, in this example into pillows, the product is dropped into a high velocity high temperature air stream conveyor in which the air is at 600F., for example, and conveyed to a cyclone separator and air lock and discharged into a third hopper. Thereafter the product is charged to a con-ventional enrober apparatus with a syrup at the ratio of 70 percent by weight of cereal pillows and 30 percent by weight syrup and admixed until a substantially uniform product is achieved wherein the resulting enrobed pro-duct is passed through a two phase oven to drop the mois-ture content to approximately 2 - 3 percent.
The coating syrup was prepared by admixing 40.8 parts of sugar (granular sucrose), 5.6 parts of coconut oil, 2.7 parts of salt, 0.1% vitamins, and 50.74 parts of water.
The product produced in accordance with Example l was tested for sensory quality against a number of com-mercially available wheat-bran based high fiber cereals.
In this test, the product of Example 1 was compared in the homes of a number of consumers against wheat-bran base high fiber products which are commercially avail-able, but which in this test were not identified to the consumer as to brand name. The product produced in ac-cordance with Example 1 was found to have a clear pref-erence over any of the products, using wheat bran as the ingredient to provide the high fiber levels. The pro-ducts of the present invention were reported to be pre-ferred with respect to flavor, texture, and bowl life.
A series of comparative tests are performed in which the procedure of Example 1 is repeated, except that in a first test of this example maize corn bran straight from the corn dry milling process is used as the maize corn bran ingredient. In a second test coarse ground maize corn bran, i.e. 100 percent through 4 mesh U.S. sieve is utilized. In the first test severe orifice plugging is encountered, surging in the extrusion, is encountered and extreme product piece disintegration is observed. By product piece disintegration I mean that the particle pieces tend to become disintegrated during the expansion step, with the result that an extremely high percentage of broken cereal pieces are produced.
In the second test of this example, the die plugging problem is greatly relieved although not elimi-nated,' severe surging continues to be observed, and again extreme cereal piece disintegration is observed.
The conditions set forth in the examples are not intended to be limiting, since the present invention is useful with any conventional cooker-extrusion expansion process for producing ready to eat cereal products.
Nonetheless, preferred ranges for the operation of the cooker-extruder otherwise in accordance with Example 1 include the use of screw speeds, for example, from about 135 - 155 rpm, manifold pressures ti.e. at the dough just upstream from the die orifices) of 2400 - 2600 psi, :` B
dough temperatures at the die of 330C- 350~F. and high velocity air stream temperatures of 600 - 700~F. are preferred in the air conveyor.
Although the example utilizes cooked cereal dough ingredients selected from oats and maize corn as the main starch source, any other cereals and cooked cereal dough ingredients are useful in the process of the present invention. For example, wheat-derived ingred-ien~s such as wheat flour, can be used, and rice, sorgum, soya, tapioca, waxy maise, and other cooked cereal dough ingredients are also useful. Sugar ingredients, flavor-ants and the like, are also added conventionally.
In accorandance with the present invention, a very desirable and satisfactory expanded ready to eat cereal product is produced utilizing the bran of maize corn. Also, the product produced therefrom was found to be of improved flavor and without wheat bran's heavy taste and texture. The product is believed to be a surprisingly desirable product inasmuch as the consumer tests which were conducted indicated that most people preferred the taste of maize corn bran over bran cereals made from wheat bran.
Thus, it is apparent from the above examples that, in accordance with the present invention, maize corn bran can be used successfully in the cooker-extruder pro-duction of expanded ready to eat cereal products providing it is first ground to the critical fineness range disclosed herein prior to incorporation of the maize corn bran as an ingredient in the manufacture of the extruded expanded cereal product. On the other hand, if maize corn bran straight from the dry milling process, or more crudely ground maize corn bran is employed a totally unsatisfactory and unworkable process results.
In accordance with the present invention, suf-ficient ground maize corn bran of the required fineness is added to the ready to eat cereal product ingredients . .
,; i : - 9 -- to provide 3.5 - 10.0 percent fiber content derived from ` corn bran. In preferred embodiments products at the range of 3.5 - 7.0 percent fiber are provided. Products in these ranges are referred to in the trade as "high fiber" products.
.
.,',; ~
.
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The present invention relates to a dry ready to eat high fiber cereal and a process of preparing the same.
Recently, there has developed increasing in-terest among nutritionists and among consumers in~high fiber food products, particularly in high fiber ready to eat cereals. At the present time, wheat bran is the principal ingredient which is relied upon to provide high fiber content for example in ready to eat cereals. How-ever, some commercially available wheat-bran ready to eat cereal products become soggy and pasty almost immediately upon wetting of the product in milk. Others are very hard and go almost to the other extreme of not being palatable, even in milk, because of prolonged hardness.
On the other hand vast quantities of maize corn bran are avaiable for use in the high fiber human food products such as, for example, ready to eat cereals. It would be highly desirable to produce high fiber cereal products utilizing maize corn bran as the source for the high fiber content, in conventional cooker-extruder ex-pansion processes and equipment, such as those disclosed in U.S. Patent 3,054,677 to W. R. Graham, Jr. et al.
or U.S. Patent 3,462,277 to R. R. Reinhardt. Such processes and equipment economically and at very high speeds, produce a modern dry, ready to eat cereal pro-duct, having an attractive palatable appearance, e.g., a bite size or larger sized product, having strong sales .
'B ~
; . ,' . :
z ~
appeal to the average consumer. The products are light, crisp and frangible, having pleasing color and taste.
In such processes a dry-appearing mixture of in-gredients is passed quickly through a cooker-extruder in which high pressure and temperature is generated. The ingredients are quickly cooked, a dough is formed, and the dough is expelled through a constricted opening, e.g.
through a plurality of dies, under high temperature and pressure conditions. Temperature and pressure ahead of the dies are maintained high enough to cause sudden release of pressure when the dough is forced through the dies, with sudden conversion of at least some of the mois-ture to steam in the extruded dough mass to develop small and large bubbles in the resulting product. This develop-ment of bubbles throughout the extrudate is called "ex-pansion." The extruded expanded dough passes through a momentary, fleeting stage in which the dough is extremely cohesive, sticky and flexible, and upon the sudden flash-ing of some additional amounts of the water, the water content drops, and the pieces are immediately transformed into less sticky pieces. The pieces are then typically charged into a high temperature, high velocity air stream, in which the drying step is completed and the dry pieces develop the highly desirable toasted appearance.
: However, the technology has not been available for the production of an extruded expanded cereal product using maize corn bran as an ingredient in such processes.
It is an object of the present invention to pro-vide process technology for the production of extruded expanded ready to eat cereal products utilizing maize corn bran as an ingredient, which product has very favorable sensory characteristics. It is a further object of the present invention to provide a high fiber expanded ready to eat cereal product utilizing maize corn bran as the principal source of the additional fiber present.
The present invention provides a process for producing a dry ready to eat high fiber cereal product comprising the steps: admixing with cereal dough ingred-ients sufficient ground maize corn bran, as an ingredient, to provide a fiber content of 3.5 to 10% by weight, based on the weight of the product, said ground maize corn bran having been ground to a fineness whereby 100 percent ofsaidgroundmaize corn passes through a 40 mesh U.S.
sieve, cooking the ingredients in a cooker-extruder to form an extrudate under temperature and pressure conditions sufficiently high to result in expansion of the dough upon its release from the cooker-extruder, cutting the expanded dough extrudate into discrete pieces, and drying the resulting pieces to a moisture level of 2-3 percent.
The present invention further provides a dry ready to eat expanded cereal product produced in a cooker-extrusion expansion process, said cereal including ground maize corn bran in an amount sufficient to provide 3.5 -10.0 percent inclusive fiber content, by weight based on the weight of the product, said ground maize corn bran having been added to said product as an ingredient which wasground to a fineness whereby 100 percent of said ground maize corn bran passes through a 40 mesh U.S. sieve.
In accordance with the present invention, an extruded expanded ready to eat cereal product utilizing maize corn bran as an ingredient to supply additional fiber, is produced in an otherwise conventional cooker-extrusion expansion p.rocess, but wherein the maize corn bran ingredient has been ground to a granulation of at least 100 percent through a 40 mesh U.S. sieve. In one preferred aspect maize corn bran ingredients having a granulation of 100 percent through a 60 mesh U.S. sieve and 70 percent through 100 mesh U.S. sieve are employed. None-theless, another preferred embodimentutilizes a granu-lation such that 100 percent passes through 40 mesh, and 45 percent stays on a 60 mesh U.S. sieve. Although I have discovered that there is no limit with respect to the amount of extremely fine particles, in fact for economic . .
,i reasons I prefer to use ingredients in which substantial portion thereof, e.g. 40 percent remains on a 60 mesh sieve.
I have found that the improved process, in ac-cordance with the present invention, is suitable for use with any type of cooked cereal dough ingredients, and in any process which utilizes a cooker-extruder, and which produces an expanded cereal product upon sudden release of pressure from the extruder through a die. There are many such processes widely known in the art, and for ex-ample those set forth in the above cited patents, and a wide range of densities are achieved in the resulting products due to the expansion into steam of the rela-tively low levels of water which are present in the dough in the extruder cooker.
Utilization of maize corn bran straight from the dry milling process in such processes was found to be totally unworkable. Such ingredients cause erratic plug-ging of the dies, surging of the dough through the extrud-er and orifices, and most significantly, results in extreme cereal piece disintegration during and after expansion.
Furthermore, coarse grinding of the maize corn bran, e.g.
so that a major portion of the ground bran just passes through 2 or 4 mesh U.S. sieve, although improving the orifice plugging problem, nonetheless results in unaccept-able surging, as well as product disintegration during and immediately after expansion. We have found that when the maize corn bran is ground to fineness at or finer than the ; levels set forth above, the orifice extrusion problem is totally eliminated, the surging problem is totally elim-inated, and the product disintegration problem during and after expansion is also eliminated. In addition, we have discovered that the resulting product has scored better than commercially available high fiber wheat-bran derived cereals when compared in consumer tests.
In the following examples all parts are expressed in parts by weight, and temperatures are expressed in degrees Fahrenheit.
! .
p~
The ingredients set forth below in Table 1 were added to a ribbon blender in the relative amounts set ` ~ forth, and were mixed until the contents of the blender appeared to be homogenous.
Yellow Maize Corn Flour 49.9 %
Ground Maize Corn Bran 25.00%
; Oat Flour 15.00%
Sugar 8.0 %
Salt 1.0 %
Soda 0-75%
Vitamin Premix 0.15~
Ground Limestone 0.17%
Color (brown) 0.02%
",~ 100. 00%
*The ground maize corn bran is maize corn bran that has been ground to a granulation of 100 percen$
through 40 mesh U.S. sieve with 45 percent on 60 ~ mesh U.S. sieve.
h +giving a fiber content of approximately 3.5~ of the whole mix.
The resulting mixture was found to contain ap-proximately 8 percent moisture. The resulting admixture is, in a separate blender, further admixed with additional quantity of makeup water so that the resulting admixture consists of approximately 20 percent total moisture. The resulting 20 percent moisture mix is freeflowing although ` it does give evidence of cohesion upon in-hand compression.
The 20 percent moisture mix is charged to an extruder cooker in which both the extruder and propulsion screw are equipped internally for water cooling. Room temperature water is circulated through both~the jacket and the screw and approximately a 10F. increase in temp-erature is encountered on the jacket although the screw coolant water exited at approximately 115 F. The extruder cooker is operated in a conventional manner to provide compression, propulsion, and extrusion of the dough, under conditions such that even though cooling is applied, the dough temperature upon extrusion is approxi-mately 340~F. with the sudden release of pressure. For example, the extrudate is passed through six orifices closely arranged in a circle in the die base and the ex-trudate from each respective orifice contacts and co-heres to extrudate on either side to form a tube. The tube is allowed to pass between conventional cutting rolls to result in individual pillow shape pieces. Typical conventional extrusion, and cutting equipment which is suitable for use in accordance with the present invention is shown in U.S. Patent 3,054,677 to W. R. Graham, Jr.
et al.
Upon the cutting of the product into pieces, in this example into pillows, the product is dropped into a high velocity high temperature air stream conveyor in which the air is at 600F., for example, and conveyed to a cyclone separator and air lock and discharged into a third hopper. Thereafter the product is charged to a con-ventional enrober apparatus with a syrup at the ratio of 70 percent by weight of cereal pillows and 30 percent by weight syrup and admixed until a substantially uniform product is achieved wherein the resulting enrobed pro-duct is passed through a two phase oven to drop the mois-ture content to approximately 2 - 3 percent.
The coating syrup was prepared by admixing 40.8 parts of sugar (granular sucrose), 5.6 parts of coconut oil, 2.7 parts of salt, 0.1% vitamins, and 50.74 parts of water.
The product produced in accordance with Example l was tested for sensory quality against a number of com-mercially available wheat-bran based high fiber cereals.
In this test, the product of Example 1 was compared in the homes of a number of consumers against wheat-bran base high fiber products which are commercially avail-able, but which in this test were not identified to the consumer as to brand name. The product produced in ac-cordance with Example 1 was found to have a clear pref-erence over any of the products, using wheat bran as the ingredient to provide the high fiber levels. The pro-ducts of the present invention were reported to be pre-ferred with respect to flavor, texture, and bowl life.
A series of comparative tests are performed in which the procedure of Example 1 is repeated, except that in a first test of this example maize corn bran straight from the corn dry milling process is used as the maize corn bran ingredient. In a second test coarse ground maize corn bran, i.e. 100 percent through 4 mesh U.S. sieve is utilized. In the first test severe orifice plugging is encountered, surging in the extrusion, is encountered and extreme product piece disintegration is observed. By product piece disintegration I mean that the particle pieces tend to become disintegrated during the expansion step, with the result that an extremely high percentage of broken cereal pieces are produced.
In the second test of this example, the die plugging problem is greatly relieved although not elimi-nated,' severe surging continues to be observed, and again extreme cereal piece disintegration is observed.
The conditions set forth in the examples are not intended to be limiting, since the present invention is useful with any conventional cooker-extrusion expansion process for producing ready to eat cereal products.
Nonetheless, preferred ranges for the operation of the cooker-extruder otherwise in accordance with Example 1 include the use of screw speeds, for example, from about 135 - 155 rpm, manifold pressures ti.e. at the dough just upstream from the die orifices) of 2400 - 2600 psi, :` B
dough temperatures at the die of 330C- 350~F. and high velocity air stream temperatures of 600 - 700~F. are preferred in the air conveyor.
Although the example utilizes cooked cereal dough ingredients selected from oats and maize corn as the main starch source, any other cereals and cooked cereal dough ingredients are useful in the process of the present invention. For example, wheat-derived ingred-ien~s such as wheat flour, can be used, and rice, sorgum, soya, tapioca, waxy maise, and other cooked cereal dough ingredients are also useful. Sugar ingredients, flavor-ants and the like, are also added conventionally.
In accorandance with the present invention, a very desirable and satisfactory expanded ready to eat cereal product is produced utilizing the bran of maize corn. Also, the product produced therefrom was found to be of improved flavor and without wheat bran's heavy taste and texture. The product is believed to be a surprisingly desirable product inasmuch as the consumer tests which were conducted indicated that most people preferred the taste of maize corn bran over bran cereals made from wheat bran.
Thus, it is apparent from the above examples that, in accordance with the present invention, maize corn bran can be used successfully in the cooker-extruder pro-duction of expanded ready to eat cereal products providing it is first ground to the critical fineness range disclosed herein prior to incorporation of the maize corn bran as an ingredient in the manufacture of the extruded expanded cereal product. On the other hand, if maize corn bran straight from the dry milling process, or more crudely ground maize corn bran is employed a totally unsatisfactory and unworkable process results.
In accordance with the present invention, suf-ficient ground maize corn bran of the required fineness is added to the ready to eat cereal product ingredients . .
,; i : - 9 -- to provide 3.5 - 10.0 percent fiber content derived from ` corn bran. In preferred embodiments products at the range of 3.5 - 7.0 percent fiber are provided. Products in these ranges are referred to in the trade as "high fiber" products.
.
.,',; ~
.
:,.
, ~ '' ...
Claims (6)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A process for producing a dry ready to eat high fiber cereal product comprising the steps: admixing with cereal dough ingredients sufficient ground maize corn bran, as an ingredient, to provide a fiber content of 3.5 to 10% by weight, based on the weight of the product, said maize corn bran having been ground to a fineness whereby 100 percent of said ground maize corn bran passes through a 40 mesh U.S. sieve, cooking the ingredients in a cooker-extruder to form an extrudate under temperature and pressure conditions sufficiently high to result in expansion of the dough upon its release from the cooker-extruder, cutting the expanded dough extrudate into discrete pieces, and drying the resulting pieces to a moisture level to 2 - 3 percent.
2. The process of Claim 1 in which said maize corn bran has been ground to a fineness whereby 100 per-cent passes through a 40 mesh U.S. sieve, and at least 45 percent remains on a 60 mesh U.S. sieve.
3. The process of Claim 1 in which maize corn bran had been ground to a fineness of 100 percent through a 60 U.S. sieve and 70 percent through a 100 mesh U.S.
sieve.
sieve.
4. The process of Claim 1, 2, or 3 in which the ground maize corn bran is added in an amount suf-ficient to provide a fiber content of 3.5 - 7.0 percent by weight, inclusive, based on the weight of the product.
5. A dry ready to eat expanded cereal product produced in a cooker-extrusion expansion process, said cereal including ground maize bran in an amount suffi-cient to provide 3.5 - 10.0 percent inclusive fiber con-tent, by weight based on the weight of the product, said ground maize corn bran having been added to said pro-duct as an ingredient which was ground to a fineness whereby 100 percent of said ground maize corn bran passes through a 40 mesh U.S. sieve.
6. The product of Claim 5 wherein all the cereal-derived ingredients are derived from oats and maize and wherein the fiber content derived from ground maize corn bran is between 3.5 - 7.0 percent by weight based on the weight of the product.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US6293479A | 1979-08-02 | 1979-08-02 | |
| US62,934 | 1979-08-02 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1115115A true CA1115115A (en) | 1981-12-29 |
Family
ID=22045813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA349,928A Expired CA1115115A (en) | 1979-08-02 | 1980-04-15 | Corn bran expanded cereal |
Country Status (12)
| Country | Link |
|---|---|
| AT (1) | AT374346B (en) |
| BE (1) | BE884470A (en) |
| CA (1) | CA1115115A (en) |
| DE (1) | DE3028975A1 (en) |
| FR (1) | FR2462106A1 (en) |
| GB (1) | GB2055545B (en) |
| IE (1) | IE49943B1 (en) |
| IT (1) | IT8049401A0 (en) |
| LU (1) | LU82676A1 (en) |
| NL (1) | NL8004403A (en) |
| NO (1) | NO150223C (en) |
| SE (1) | SE8005520L (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130243925A1 (en) * | 2012-03-13 | 2013-09-19 | Bernhard H. van Lengerich | Cereal-Based Product with Improved Eating Quality Fortified with Dietary Fiber and/or Calcium |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2178637A (en) * | 1985-06-22 | 1987-02-18 | D & S Food Prod Ltd | Food product and process for making it |
| DE3711840A1 (en) * | 1987-04-08 | 1988-10-27 | Schaaf Ohg Heinz | METHOD FOR PRODUCING EXPANDED FOOD |
| IE60531B1 (en) * | 1987-09-09 | 1994-07-27 | Food & Cereal Research | A process for manufacturing a reconstitutable oat cereal |
| US5169662A (en) * | 1989-08-31 | 1992-12-08 | New Generation Foods, Inc. | Dietary product and method for manufacture |
| ME03021B (en) | 2015-10-16 | 2018-10-20 | Gold&Green Foods Oy | A method of manufacturing a textured food product and a texturized food product |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3054677A (en) * | 1959-06-26 | 1962-09-18 | Quaker Oats Co | Method of making shredded cereal product |
| US3476567A (en) * | 1966-03-21 | 1969-11-04 | Helme Products Inc | Process for preparing expanded cornmeal extrusions |
| ZA764365B (en) * | 1975-08-27 | 1977-07-27 | Gen Mills Inc | Snack food process |
| GB1570521A (en) * | 1976-02-09 | 1980-07-02 | Golden Wonder Ltd | Extrusion process for the treatment of cereal |
| FR2432842A2 (en) * | 1978-08-09 | 1980-03-07 | Sodes Sa | Food prods contg. bran, gluten and flour - prepd. continuously by extruding mixt. with water; used in diet bread, cereals, etc. |
| DE2837294A1 (en) * | 1977-08-29 | 1979-03-15 | Sodes Sa | Food prods contg. bran, gluten and flour - prepd. continuously by extruding mixt. with water; used in diet bread, cereals, etc. |
| 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. |
| GB1561190A (en) * | 1977-12-20 | 1980-02-13 | Weetabix Ltd | Process for cooking and extruding food mixtures |
-
1980
- 1980-03-26 GB GB8010216A patent/GB2055545B/en not_active Expired
- 1980-04-15 CA CA349,928A patent/CA1115115A/en not_active Expired
- 1980-07-16 IE IE1473/80A patent/IE49943B1/en unknown
- 1980-07-24 FR FR8016321A patent/FR2462106A1/en not_active Withdrawn
- 1980-07-25 BE BE1/9904A patent/BE884470A/en not_active IP Right Cessation
- 1980-07-30 DE DE19803028975 patent/DE3028975A1/en not_active Withdrawn
- 1980-07-31 NL NL8004403A patent/NL8004403A/en not_active Application Discontinuation
- 1980-08-01 AT AT0400880A patent/AT374346B/en not_active IP Right Cessation
- 1980-08-01 LU LU82676A patent/LU82676A1/en unknown
- 1980-08-01 SE SE8005520A patent/SE8005520L/en not_active Application Discontinuation
- 1980-08-01 NO NO802316A patent/NO150223C/en unknown
- 1980-08-01 IT IT8049401A patent/IT8049401A0/en unknown
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130243925A1 (en) * | 2012-03-13 | 2013-09-19 | Bernhard H. van Lengerich | Cereal-Based Product with Improved Eating Quality Fortified with Dietary Fiber and/or Calcium |
| US9560877B2 (en) * | 2012-03-13 | 2017-02-07 | General Mills, Inc. | Cereal-based product with improved eating quality fortified with dietary fiber and/or calcium |
| US10004254B2 (en) | 2012-03-13 | 2018-06-26 | General Mills, Inc. | Cereal-based product with improved eating quality fortified with dietary fiber and/or calcium |
Also Published As
| Publication number | Publication date |
|---|---|
| SE8005520L (en) | 1981-02-03 |
| NO150223C (en) | 1984-09-12 |
| GB2055545B (en) | 1983-06-22 |
| IE49943B1 (en) | 1986-01-08 |
| NO150223B (en) | 1984-06-04 |
| IT8049401A0 (en) | 1980-08-01 |
| AT374346B (en) | 1984-04-10 |
| NL8004403A (en) | 1981-02-04 |
| FR2462106A1 (en) | 1981-02-13 |
| IE801473L (en) | 1981-02-02 |
| ATA400880A (en) | 1983-09-15 |
| BE884470A (en) | 1981-01-26 |
| GB2055545A (en) | 1981-03-11 |
| DE3028975A1 (en) | 1981-02-26 |
| LU82676A1 (en) | 1981-03-24 |
| NO802316L (en) | 1981-02-03 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MKEX | Expiry |